Method for producing and purifying 2,3,3,3-tetrafluoro-1-propene

ABSTRACT

The invention relates to a method for producing and purifying 2,3,3,3-tetrafluoro-1-propene using a first composition comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), and trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), said method comprising the steps of: (a) bringing said first composition into contact with at least one organic extraction agent in order to form a second composition; (b) extractive distillation of said second composition in order to form (i) a third composition comprising said organic extraction agent, 3,3,3-trifluoropropene (1243zf), and trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), and (ii) a stream comprising the 2,3,3,3-tetrafluoro-1-propene; and (c) recovery and separation of said third composition in order to form a stream comprising said organic extraction agent and a stream comprising 3,3,3-trifluoropropene (1243zf) and trans-1,3,3,3-tetra-fluoro-1-propene (1234ze-E).

TECHNICAL FIELD OF THE INVENTION

The invention relates to a process for purifying 2,3,3,3-tetrafluoro-1-propene. The invention also relates to a process for producing and purifying 2,3,3,3-tetrafluoro-1-propene.

TECHNOLOGICAL BACKGROUND OF THE INVENTION

Hydrofluorocarbons (HFCs) and in particular hydrofluoroolefins (HFOs), such as 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf), are compounds known for their properties as coolants, heat-transfer fluids, extinguishers, propellants, foaming agents, swelling agents, gaseous dielectrics, polymerization medium or monomer, support fluids, agents for abrasives, drying agents and fluids for power production units. HFOs have been identified as desirable alternatives to HCFC on account of their low ODP (ozone depletion potential) and GWP (global warming potential) values.

Most of the processes for manufacturing hydrofluoroolefins involve a fluorination and/or dehydrohalogenation reaction. These reactions are performed in the gas phase and generate impurities which consequently need to be removed to obtain the desired compound in a sufficient degree of purity for the targeted applications.

For example, in the context of producing 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf), the presence of impurities such as 1-chloro-3,3,3-trifluoro-1-propene (1233zd), 1,3,3,3-tetrafluoro-1-propene (1234ze) and 1,1,1,3,3-pentafluoropropane (245fa) is observed. These impurities are isomers of the main compounds that are desired to be obtained via the process for producing 2,3,3,3-tetrafluoro-1-propene, besides the latter, i.e. 2-chloro-3,3,3-trifluoro-1-propene (1233xf) and 1,1,1,2,2-pentafluoropropane (245cb). Given the respective boiling points of 1-chloro-3,3,3-trifluoro-1-propene (1233zd), 1,3,3,3-tetrafluoro-1-propene (1234ze) and 1,1,1,3,3-pentafluoropropane (245fa), they may accumulate in the reactor and thus prevent the formation of the products of interest.

Purification of this type of reaction mixture may be performed via various techniques known from the prior art, for instance distillation. However, when the compounds to be purified have boiling points that are too close or when they form azeotropic or quasi-azeotropic compositions, distillation is not an efficient process. Extractive distillation processes have thus been described.

EP 0 864 554 discloses a process for purifying a mixture comprising 1,1,1,3,3-pentafluoropropane (245fa) and 1-chloro-3,3,3-trifluoro-trans-1-propene (1233zd) by distillation in the presence of a solvent with a boiling point of greater than that of 1-chloro-3,3,3-trifluoro-trans-1-propene.

WO 03/068716 discloses a process for recovering pentafluoroethane from a mixture comprising pentafluoroethane and chloropentafluoroethane by distillation in the presence of hexafluoropropene.

WO 98/19982 also discloses a process for purifying 1,1-difluoroethane by extractive distillation. The process consists in placing an extracting agent in contact with a mixture of 1,1-difluoroethane and vinyl chloride. The extracting agent is chosen from hydrocarbons, alcohols and chlorocarbons with a boiling point of between 10° C. and 120° C.

As mentioned by WO 98/19982, the selection of the extracting agent may prove to be complex depending on the products to be separated. There is thus still a need to develop a particular process for purifying 2,3,3,3-tetrafluoro-1-propene.

SUMMARY OF THE INVENTION

In a process for producing 2,3,3,3-tetrafluoro-1-propene, the choice of particular operating conditions makes it possible to promote the presence of certain impurities or of isomers thereof. The presence of impurities such as 1,3,3,3-tetrafluoro-1-propene (1234ze) may be observed, as may that of 1-chloro-3,3,3-trifluoro-1-propene (1233zd) and 1,1,1,3,3-pentafluoropropane (245fa). These impurities may derive from side reactions induced by intermediate compounds produced during the production of 2,3,3,3-tetrafluoro-1-propene, and may have physical properties such that the removal thereof may prove to be complex. The present invention allows the production of 2,3,3,3-tetrafluoro-1-propene in improved purity.

According to a first aspect, the present invention provides a process for purifying 2,3,3,3-tetrafluoro-1-propene (1234yf) using a first composition comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), said process comprising the steps of:

-   -   a) placing said first composition in contact with at least one         organic extracting agent to form a second composition;     -   b) extractive distillation of said second composition to form:         -   i) a third composition comprising said organic extracting             agent, 3,3,3-trifluoropropene (1243zf),             trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and             optionally or not at least one compound chosen from the             group consisting of chloromethane (40), 1,1-difluoroethane             (152a), chloropentafluoroethane (115),             1,1,1,2-tetrafluoroethane (134a) and             trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and         -   ii) a stream comprising 2,3,3,3-tetrafluoro-1-propene;     -   c) recovery and separation of said third composition to form a         stream comprising said organic extracting agent and a stream         comprising 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one compound chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E); preferably,         the stream comprising said organic extracting agent is recycled         into step a).

Preferably, the stream comprising 2,3,3,3-tetrafluoro-1-propene formed in step a b) is recovered. This stream may be optionally purified to achieve a degree of purity suitable for particular commercial specifications.

According to a preferred embodiment, said organic extracting agent is a solvent chosen from the group consisting of hydrocarbon, halohydrocarbon, alcohol, ketone, amine, ester, ether, aldehyde, nitrile, carbonate, thioalkyl, amide and heterocycle; or said organic extracting agent is difluoroethylsilane, triethylfluorosilane or perfluorobutanoic acid; preferably, said organic extracting agent is a solvent chosen from the group consisting of ketone, ester, aldehyde, ether, carbonate and heterocycle.

According to a preferred embodiment, said organic extracting agent has a boiling point of between 10 and 150° C.

According to a preferred embodiment, said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/(γ_(2,S)*P2) in which

-   -   γ_(1,S) represents the activity coefficient of         2,3,3,3-tetrafluoro-1-propene in said organic extracting agent         at infinite dilution;     -   P1 represents the saturating vapor pressure of         2,3,3,3-tetrafluoro-1-propene;     -   γ_(2,S) represents the activity coefficient of         3,3,3-trifluoropropene (1243zf) or         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic         extracting agent at infinite dilution;     -   P2 represents the saturating vapor pressure of         3,3,3-trifluoropropene (1243zf) or         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E);         advantageously, the separation factor is greater than or equal         to 1.2, preferably greater than or equal to 1.4, more         preferentially greater than or equal to 1.6, in particular         greater than or equal to 1.8, more particularly greater than or         equal to 2.0.

According to a preferred embodiment, said organic extracting agent has an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) or trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution; advantageously, the absorption capacity C_(2,S) is greater than or equal to 0.40, preferably greater than or equal to 0.60, more preferentially greater than or equal to 0.80, in particular greater than or equal to 1.0.

According to a preferred embodiment, said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene, γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution and P2 represents the saturating vapor pressure of 3,3,3-trifluoropropene (1243zf); and said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene, γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution and P2 represents the saturating vapor pressure of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E); advantageously, said organic extracting agent has a separation factor of greater than or equal to 1.2, preferably greater than or equal to 1.4, more preferentially greater than or equal to 1.6, in particular greater than or equal to 1.8, more particularly greater than or equal to 2.0.

According to a preferred embodiment, said organic extracting agent may have an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution; and said organic extracting agent may have an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution; advantageously, the absorption capacity C_(2,S) is greater than or equal to 0.40, preferably greater than or equal to 0.60, more preferentially greater than or equal to 0.80, in particular greater than or equal to 1.0.

According to a preferred embodiment, said first composition is an azeotropic or quasi-azeotropic composition comprising 2,3,3,3-tetrafluoro-1-propene, trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), 3,3,3-trifluoropropene (1243zf) and optionally or not at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

According to a preferred embodiment, said organic extracting agent is chosen from the group consisting of 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, n-propyl formate, 1,2-dimethoxyethane, isopropyl acetate, 2-methylbutanal, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 1-methylpiperazine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate, and 1-propoxy-2-propanol; advantageously, said organic extracting agent is chosen from the group consisting of ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, 1,2-dimethoxyethane, isopropyl acetate, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butyl acetate, 1-ethoxy-2-propanol and hexanal; preferably, said organic extracting agent is chosen from the group consisting of dimethoxymethane, butanone, isopropyl acetate, dioxane, trimethoxymethane, 1,3-dioxane, n-butyl acetate, 1-ethoxy-2-propanol and hexanal; in particular, said organic extracting agent is chosen from the group consisting of dimethoxymethane, isopropyl acetate, dioxane, trimethoxymethane, 1,3-dioxane, n-butyl acetate, 1-ethoxy-2-propanol and hexanal.

According to a preferred embodiment, the stream comprising 2,3,3,3-tetrafluoro-1-propene formed in step b) is recovered and is free of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and/or of 3,3,3-trifluoropropene (1243zf) and/or of at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

According to a preferred embodiment, said first composition comprises impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene and optionally heavy impurities, and the process comprises, prior to step a), the following steps:

-   -   i′) use or provision of a composition comprising         2,3,3,3-tetrafluoro-1-propene, impurities with a boiling point         below the boiling point of 2,3,3,3-tetrafluoro-1-propene,         3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one compound chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and         optionally heavy impurities;     -   ii′) distillation of said composition from step i) to remove, at         the top of the column, impurities with a boiling point below the         boiling point of 2,3,3,3-tetrafluoro-1-propene and to form a         first stream comprising 2,3,3,3-tetrafluoro-1-propene,         3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one compound chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and         optionally heavy impurities; recovered at the bottom of the         distillation column;     -   iii′) optionally, distillation of said first stream recovered at         the bottom of the distillation column in step ii′) to recover,         at the top of the column, a second stream comprising         2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one compound chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and, at the         bottom of the distillation column, a stream comprising the heavy         impurities;     -   said at first stream recovered in step ii′) or said second         stream recovered in step iii′) corresponding to said first         composition used in step a).

The heavy impurities may contain, for example, 1,1,1,3,3,3-hexafluoropropane (236fa), 1,1,1,2,3,3-hexafluoropropane (236ea), 1,1,1,2,3,3,3-heptafluoropropane (227ca), cis-1,3,3,3-tetrafluoro-1-propene (1234ze-Z), and dimers or trimers derived from one of the compounds present in the composition or the stream under consideration, for example C4 or C5 hydrocarbons such as hexafluorobutene (1336), heptafluorobutene (1327), octafluorobutane (338), nonafluoropentene (1429) or heptafluoropentene (1447).

According to a second aspect of the present invention, a process for producing 2,3,3,3-tetrafluoro-1-propene is provided. Said process comprises the steps of:

-   -   A) fluorination in the presence of a catalyst of a compound of         formula CX(Y)₂−CX(Y)_(m)−CH_(m)XY (I) in which X and Y         independently represent H, F or Cl and m=0 or 1; and/or         fluorination in the presence of a catalyst of a compound of         formula (CX_(n)Y_(3−n))CH_(p)X_(1−p)CH_(m)X_(2−m) (II) in which         X is, independently of each other, Cl, F, I or Br; Y is,         independently of each other, H, Cl, F, I or Br; n is 1, 2 or 3;         and m is 0, 1 or 2; and p is 0 or 1;     -   B) recovery of a stream comprising         2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one compound chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E);     -   C) implementation of the process as claimed in any one of claims         1 to 9 using the stream recovered in step B).

According to another aspect, the present invention provides a composition comprising 2,3,3,3-tetrafluoropropene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and an organic extracting agent having:

-   -   a separation factor S_(1,2) of greater than or equal to 1.40,         said separation factor being calculated by the formula         S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the         activity coefficient of 2,3,3,3-tetrafluoropropene in said         organic extracting agent at infinite dilution, P1 represents the         saturating vapor pressure of 2,3,3,3-tetrafluoropropene, γ_(2,S)         represents the activity coefficient of 3,3,3-trifluoropropene         (1243zf) in said organic extracting agent at infinite dilution,         P2 represents the saturating vapor pressure of         3,3,3-trifluoropropene (1243zf) and     -   a separation factor S_(1,2) of greater than or equal to 1.40,         said separation factor being calculated by the formula         S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the         activity coefficient of 2,3,3,3-tetrafluoropropene in said         organic extracting agent at infinite dilution, P1 represents the         saturating vapor pressure of 2,3,3,3-tetrafluoropropene, γ_(2,S)         represents the activity coefficient of         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic         extracting agent at infinite dilution, P2 represents the         saturating vapor pressure of trans-1,3,3,3-tetrafluoro-1-propene         (1234ze-E);

preferably, said organic extracting agent has:

an absorption capacity C_(2,S) of greater than or equal to 0.60, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution; and an absorption capacity C_(2,S) of greater than or equal to 0.60, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution.

Preferably, the organic extracting agent is chosen from the group consisting of acetaldehyde, methyl formate, 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, 1-chloro-1,2,2-trifluoropropane, 3-chloro-1,1,1-trifluoropropane, ethanedial, 2-chloro-1,1,1,3-tetrafluoropropane, propanone, methyl acetate, 4-methoxy-2-methyl-2-butanethiol, difluorodiethylsilane, isobutanal, isopropyl formate, methylglyoxal, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, butanone, n-propyl formate, 1,3-dichloro-1,1,2-trifluoropropane, 1,1-dichloro-2,2,3-trifluoropropane, 1,2-dimethoxyethane, 1,3-dichloro-1,2,2-trifluoropropane, isopropyl acetate, diethyl sulfide, 1,3-dichloro-1,2,3-trifluoropropane, 2-methylbutanal, 2-allyloxyethanol, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, pyridine, n-methylmorpholine, 4-methyl-2-pentanone, butyronitrile, 1-methoxy2-propanol, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 2-methoxy1-propanol, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-methylpiperazine, n-ethylmorpholine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate, 2-propoxyethanol and 1-propoxy-2-propanol.

BRIEF DESCRIPTION OF THE FIGURES

FIGS. 1a-c schematically represent a device for performing a process for purifying 2-3,3,3-tetrafluoro-1-propene according to a particular embodiment of the present invention.

FIG. 2 schematically represents a device for performing a process for producing 2,3,3,3-tetrafluoro-1-propene according to a particular embodiment of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

The term “hydrocarbon” as used herein refers to linear or branched C₁-C₂₀ alkane, C₃-C₂₀ cycloalkane, C₅-C₂₀ alkene, C₅-C₂₀ cycloalkene or C₆-C₁₈ arene compounds. For example, the term “alkane” refers to compounds of formula C_(n)H_(2n+2) in which n is between 1 and 20. The term “C₁-C₂₀ alkane” includes, for example, pentane, hexane, heptane, octane, nonane and decane, or isomers thereof. The term “C₅-C₂₀ alkene” refers to hydrocarbon-based compounds comprising one or more carbon-carbon double bonds and comprising from 5 to 20 carbon atoms. The term “C₃-C₂₀ cycloalkane” refers to a saturated hydrocarbon-based ring comprising from 3 to 20 carbon atoms. The term “C₆-C₁₈ aryl” refers to cyclic and aromatic hydrocarbon-based compounds comprising from 6 to 18 carbon atoms. The term “C₅-C₂₀ cycloalkene” refers to cyclic hydrocarbon-based compounds comprising from 5 to 20 carbon atoms and comprising one or more carbon-carbon double bonds.

The term “alkyl” denotes a monovalent radical derived from a linear or branched alkane, comprising from 1 to 20 carbon atoms. The term “cycloalkyl” denotes a monovalent radical derived from a cycloalkane, comprising from 3 to 20 carbon atoms. The term “aryl” denotes a monovalent radical derived from an arene, comprising from 6 to 18 carbon atoms. The term “alkenyl” denotes a monovalent radical of 2 to 20 carbon atoms and at least one carbon-carbon double bond. The term “alkynyl” denotes a monovalent radical of 2 to 20 carbon atoms and at least one carbon-carbon triple bond. The term “halogen” refers to an —F, —Cl, —Br or —I group. The term “cycloalkenyl” refers to a monovalent radical derived from a cycloalkene comprising from 3 to 20 carbon atoms. The C₁-C₂₀ alkyl, C₂-C₂₀ alkenyl, C₂-C₂₀ alkynyl, C₃-C₂₀ cycloalkyl, C₃-C₂₀ cycloalkenyl and C₆-C₁₈ aryl substituents may be optionally substituted with one or more —OH, halogen, —NR^(a) C(O)R^(b), —C(O)NR^(a)R^(b)—CN, —NO₂, —NR^(a)R^(b), —OR^(a),—SR^(a), —CO₂R^(a), —OC(O)OR^(a), —OC(O)R^(a), —C(O)H or —C(O)R^(a) substituents in which R^(a) and R^(b) are, independently of each other, hydrogen, unsubstituted C₁-C₂₀ alkyl, unsubstituted C₂-C₂₀ alkenyl, unsubstituted C₂-C₂₀ alkynyl, unsubstituted C₃-C₂₀ cycloalkyl, unsubstituted C₃-C₂₀ cycloalkenyl or unsubstituted C₆-C₁₈ aryl. In the substituents —NR^(a)R^(b), R^(a) and R^(b) may form, with the nitrogen atom to which they are attached, a saturated or unsaturated, aromatic or non-aromatic, 5- to 10-membered heterocycle.

The term “halohydrocarbons” refers to compounds of formula R^(a)X in which R^(a) is chosen from C₁-C₂₀ alkyl, C₂-C₂₀ alkenyl, C₂-C₂₀ alkynyl, C₃-C₂₀ cycloalkyl, C₃-C₂₀ cycloalkenyl and C₆-C₁₈ aryl and X represents a chlorine, fluorine, bromine or iodine atom. The C₁-C₂₀ alkyl, C₂-C₂₀ alkenyl, C₂-C₂₀ alkynyl, C₃-C₂₀ cycloalkyl, C₃-C₂₀ cycloalkenyl and C₆-C₁₈ aryl substituents may be optionally substituted with one or more —OH, halogen, —NR^(a) C(O)R^(b), —C(O)NR^(a)R^(b)—CN, —NO₂, —NR^(a)R^(b), —OR^(a), —SR^(a), —CO₂R^(a), —OC(O)OR^(a), —OC(O)R^(a), —C(O)H or —C(O)R^(a) substituents in which R^(a) and R^(b) are as defined above.

The term “alcohol” refers to hydrocarbons or halohydrocarbons as defined above in which at least one hydrogen atom is replaced with a hydroxyl group —OH.

The term “ketone” refers to hydrocarbons comprising at least one or more carbonyl functional groups R^(c)—C(O)—R^(d) in which R^(c) and R^(d) are, independently of each other, a C₁-C₂₀ alkyl, C₂-C₂₀ alkenyl, C₂-C₂₀ alkynyl, C₃-C₂₀ cycloalkyl, C₃-C₂₀ cycloalkenyl or C₆-C₁₈ aryl and may be optionally substituted with one or more —OH, halogen, —NR^(a) C(O)R^(b), —C(O)NR^(a)R^(b)—CN, —NO₂, —NR^(a)R^(b), —OR^(a), —SR^(a), —CO₂R^(a), —OC(O)OR^(a), —OC(O)R^(a), —C(O)H or —C(O)R^(a) substituents in which R^(a) and R^(b) are defined above, R^(c) and R^(d) possibly being linked together to form, with the carbonyl group to which they are attached, a 4- to 10-membered and preferably 4- to 7-membered cyclic ketone. The cyclic ketone may also comprise one or more carbon-carbon double bonds. The cyclic ketone may also be optionally substituted with one or more substituents as defined above.

The term “amine” refers to hydrocarbons comprising at least one or more amine functional groups —NR^(c)R^(d) in which R^(c) and R^(d) are as defined above, R^(c) and R^(d) possibly being linked together to form, with the nitrogen atom to which they are attached, a 4- to 10-membered aromatic or non-aromatic heterocycle.

The term “esters” refers to compounds of formula R^(c)—C(O)—O—R^(d) in which R^(c) and R^(d) are as defined above, R^(c) and R^(d) possibly being linked together to form, with the ester group, a ring comprising from 4 to 20 carbon atoms.

The term “ether” refers to compounds of formula R^(c)—O—R^(d) in which R^(c) and R^(d) are as defined above, R^(c) and R^(d) possibly being linked together to form, with the oxygen atom to which they are attached, a heterocycle comprising from 4 to 20 carbon atoms.

The term “aldehyde” refers to compounds comprising at least one or more —C(O)—H functional groups.

The term “nitrile” refers to compounds comprising at least one or more —CN functional groups.

The term “carbonate” refers to compounds of formula R^(c)—O—C(O)—O—R^(d) in which R^(c) and R^(d) are as defined above.

The term “thioalkyl” refers to compounds of formula R^(c)SR^(d) in which R^(c) and R^(d) are as defined above.

The term “amide” relates to compounds of formula R^(c)C(O)NR^(e)R^(d) in which R^(c) and R^(d) are as defined above, R^(e): being defined by the same substituents as R^(c), R^(c) and R^(d) possibly being linked together to form, with the amide group —C(O)N— to which they are attached, a 4- to 10-membered and preferably 4- to 7-membered cyclic amide. The cyclic amide may also comprise one or more carbon-carbon double bonds. The cyclic amide may also be optionally substituted with one or more substituents as defined above.

The term “heterocycle” denotes a 4- to 10-membered carbon-based ring, at least one of the ring members of which is a heteroatom chosen from the group consisting of O, S, P and N. The ring may comprise one or more carbon-carbon double bonds or one or more carbon-heteroatom double bonds or one or more heteroatoms-heteroatom double bonds. Preferably, the heterocycle may comprise 1, 2, 3, 4 or 5 heteroatoms as defined above. In particular, the heterocycle may comprise 1, 2 or 3 heteroatoms chosen from oxygen, nitrogen and sulfur. Preferably, the heterocycle may be a 4- to 6-membered carbon-based ring, 1, 2 or 3 ring members of which are heteroatoms chosen from O and N. The heterocycle may be optionally substituted with one or more substituents chosen from —OH, halogen, —NR^(a) C(O)R^(b), —C(O)NR^(a)R^(b)—CN, —NO₂, —NR^(a)R^(b), —OR^(a), —SR^(a), —CO₂R^(a), —OC(O)OR^(a), —OC(O)R^(a), —C(O)H and —C(O)R^(a) in which R^(a) and R^(b) are as defined above.

The term “azeotropic composition” denotes a liquid mixture of two or more compounds which behave like a single substance, and which boils at a fixed temperature maintaining a composition in the liquid phase identical to that in the gas phase. The term “quasi-azeotropic composition” denotes a liquid mixture of two or more compounds having a constant boiling point or which has a tendency not to fractionate when it is subjected to boiling or to evaporation.

The term “organic extracting agent” refers to a compound comprising at least one carbon atom.

According to a first aspect, the invention relates to a process for purifying 2,3,3,3-tetrafluoro-1-propene (1234yf). The purification process is performed using a first composition comprising 2,3,3,3-tetrafluoro-1-propene and at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf).

Said process may comprise the steps of:

-   -   a) placing said first composition in contact with at least one         organic extracting agent to form a second composition;     -   b) extractive distillation of said second composition to form:         -   i) a third composition comprising said organic extracting             agent and at least one compound chosen from the group             consisting of chloromethane (40), 1,1-difluoroethane (152a),             chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane             (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),             trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and             3,3,3-trifluoropropene (1243zf); and         -   ii) a stream comprising 2,3,3,3-tetrafluoro-1-propene;     -   c) recovery and separation of said third composition to form a         stream comprising said organic extracting agent and a stream         comprising at least one compound chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf).

Preferably, the stream comprising said organic extracting agent is recycled into step a).

Advantageously, said first composition may comprise 2,3,3,3-tetrafluoro-1-propene and at least two, at least three, at least four, at least five, at least six or all of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf); and said third composition may comprise at least two, at least three, at least four, at least five, at least six or all of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf).

Preferably, said first composition may comprise 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf) and at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and thus, said third composition may comprise 3,3,3-trifluoropropene (1243zf) and at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

In particular, said first composition may comprise 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and said third composition may comprise 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

Thus, said process may comprise the steps of:

-   -   a) placing said first composition in contact with at least one         organic extracting agent to form a second composition;     -   b) extractive distillation of said second composition to form:         -   i) a third composition comprising said organic extracting             agent, 3,3,3-trifluoropropene (1243zf),             trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and             optionally or not at least one compound chosen from the             group consisting of chloromethane (40), 1,1-difluoroethane             (152a), chloropentafluoroethane (115),             1,1,1,2-tetrafluoroethane (134a) and             trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and         -   ii) a stream comprising 2,3,3,3-tetrafluoro-1-propene;     -   c) recovery and separation of said third composition for a         stream comprising said organic extracting agent and a stream         comprising 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one compound chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

Said first composition may comprise between 75% and 99.99% by weight of 2,3,3,3-tetrafluoro-1-propene relative to the total weight of the first composition, advantageously between 80% and 99.9% by weight, preferably between 85% and 99.8% and in particular between 90% and 99.5% by weight of 2,3,3,3-tetrafluoro-1-propene relative to the total weight of the first composition.

When it contains same, said first composition may comprise between 0 and 2000 ppm by weight of 1,1-difluoroethane (152a) relative to the total weight of the first composition, advantageously between 0 and 1000 ppm by weight, preferably between 0 and 500 ppm and in particular between 0 and 250 ppm by weight of 1,1-difluoroethane (152a) relative to the total weight of the first composition.

When it contains same, said first composition may comprise between 0.01% and 25% by weight of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) relative to the total weight of the first composition, advantageously between 0.1% and 20% by weight, preferably between 0.2% and 15%, in particular between 0.5% and 10% by weight and more particularly between 3% and 10% by weight of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) relative to the total weight of the first composition.

When it contains same, said first composition may comprise less than 2000 ppm by weight of 1,1,1,2-tetrafluoroethane (134a) relative to the total weight of the first composition, advantageously between 1 and 1000 ppm by weight, preferably between 1 and 500 ppm and in particular between 1 and 250 ppm by weight of 1,1,1,2-tetrafluoroethane (134a) relative to the total weight of the first composition.

When it contains same, said first composition may comprise less than 1% by weight of chloromethane (40) relative to the total weight of the first composition, advantageously between 1 and 5000 ppm by weight, preferably between 1 and 2000 ppm and in particular between 10 and 1500 ppm by weight of chloromethane (40) relative to the total weight of the first composition.

When it contains same, said first composition may comprise less than 2000 ppm by weight of chloropentafluoroethane (115) relative to the total weight of the first composition, advantageously between 1 and 1000 ppm by weight, preferably between 1 and 500 ppm and in particular between 1 and 250 ppm by weight of chloropentafluoroethane (115) relative to the total weight of the first composition.

When it contains same, said first composition may comprise less than 2000 ppm by weight of cis-1,2,3,3,3-pentafluoropropene (1225ye) relative to the total weight of the first composition, advantageously between 1 and 1000 ppm by weight, preferably between 1 and 500 ppm and in particular between 1 and 250 ppm by weight of cis-1,2,3,3,3-pentafluoropropene (1225ye-Z) relative to the total weight of the first composition.

When it contains same, said first composition may comprise less than 1% by weight of 1,1,1-trifluoropropene (1243zf) relative to the total weight of the first composition, advantageously between 0 and 5000 ppm by weight, preferably between 1 and 2000 ppm and in particular between 1 and 1500 ppm by weight of 1,1,1-trifluoropropene (1243zf) relative to the total weight of the first composition.

According to a particular embodiment, said organic extracting agent is a solvent chosen from the group consisting of hydrocarbon, halohydrocarbon, alcohol, ketone, amine, ester, ether, aldehyde, nitrile, carbonate, sulfoxide, sulfate, thioalkyl, amide and heterocycle; or said organic extracting agent is difluoroethylsilane, triethylfluorosilane perfluorobutanoic acid. Preferably, said organic extracting agent is a solvent chosen from the group consisting of ketone, ester, aldehyde, ether, carbonate and heterocycle. Preferably, the heterocycle may be a 4- to 6-membered carbon-based ring, 1, 2 or 3 ring members of which are heteroatoms chosen from O and N.

Preferably, the hydrocarbons are chosen from the group consisting of 2,2-dimethylbutane, 3-methylpentane, hexane, 2,4-dimethylpentane, cyclohexane, cyclohexene, methylcyclohexane, 2,4,4-trimethyl-1-pentene, 2,2,4-trimethyl-2-pentene, 1-methylcyclohexene, toluene, 2,3-dimethylhexane, octane, ethylcyclohexane, ethylbenzene, 1,4-dimethylbenzene, 1,3-dimethylbenzene, 1,2,3-trimethylcyclohexane, 1,2-dimethylbenzene and styrene.

Preferably, the hydrocarbons are chosen from the group consisting of chloroethane, 3-chloro-1,1,1,2,2,3-hexafluoropropane, 2-chloro-1,1,1,3,3,3-hexafluoropropane, 1,1,1,3,3-pentafluoropropane, bromofluoromethane, 1-bromo-1,2-difluoroethylene, 1-chloro-1,1,2,3,3,3-hexafluoropropane, 1-chloro-1,1,2,2-tetrafluoropropane, 1-chloro-1,1,2,2,3,3-hexafluoropropane, 2-chloro-1,1,1,2-tetrafluoropropane, 1,1,1,2,3-pentafluoropropane, trichlorofluoromethane, 1-chloro-1,1-difluoropropane, 1,1,1-trifluoro-2-bromoethane, 1,1-dichloro-2,2,2-trifluoroethane, 1-chloro-2,2,3,3,3-pentafluoropropane, 1,2-dichloro-1,1,2-trifluoroethane, 1,1-dichloroethylene, 1,1,1,2,3,4,4,4-octafluorobutane, 2-chloro-2-fluoropropane, 1-chloro-2,2-difluoroethane, 2-chloropropane, bromoethane, dichloromethane, 2-chloro-1,1,1,3,3-pentafluoropropane, 1-chloro-1,2,2-trifluoropropane, iodomethane, 2,2-dichloro-1,1,1,3,3-pentafluoropropane, 3-chloropropene, 3-chloro-1,1,1-trifluoropropane, 1,1,1-trichloro-2,2,2-trifluoroethane, 1,2-dichloro-1,2-difluoroethane, 1,2-dichloro-1,1,2,3,3-pentafluoropropane, 1,1,2-trichloro-1,2,2-trifluoroethane, 1,2-dichloro-1,1,3,3,3-pentafluoropropane, 1-chloro-1,2,2,3-tetrafluoropropane, 1,1-dichloro-1,2,2,3,3-pentafluoropropane, 2-chloro-2-methylpropane, 3-chloro-1,1,1,3-tetrafluoropropane, 2,3-dichloro-1,1,1,2,3-pentafluoropropane, 1,1-dichloro-2,2,3,3,3-pentafluoropropane, 2-chloro-1,1,1,3-tetrafluoropropane, 1,3-dichloro-1,1,2,3,3-pentafluoropropane, 1,2-dichloro-3,3,3-trifluoropropene, 1,3-dichloro-1,1,2,2,3-pentafluoropropane, 1,1,1,2,2,3,4,5,5,5-decafluoropentane, 2,2-dichloro-1,1,1,3-tetrafluoropropane, 1-chloro-2,2-difluoropropane, 1,1-dichloroethane, 2-bromopropane, 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane, 1,1-dichloro-2,2-difluoroethane, 2,2-dichloro-1,1,3,3-tetrafluoropropane, trichloromethane, 2,3-dichloro-1,1,1,2-tetrafluoropropane, 1,1-dichloro-1,2,2,3-tetrafluoropropane, 1,3-dichloro-1,1,2,2-tetrafluoropropane, 1,1,1-trichloro-2,2-difluoroethane, 1,2-dichloro-1,2,3,3-tetrafluoropropane, chlorobromomethane, 2-chlorobutane, 1,3-dichloro-1,1,3,3-tetrafluoropropane, 1,3-dichloro-1,2,2,3-tetrafluoropropane, 1,2-dichloro-1,1,2,3-tetrafluoropropane, 3-bromopropene, 2,3-dichloro-1,1,1,3-tetrafluoropropane, 1,1-dichloro-2-fluoroethane, 1-bromopropane, 1,1-difluoro-1,2,2-trichloroethane, 1,1,2-trichloro-1,2-difluoroethane, iodoethane, 2-bromo-2-methylpropane, 1,2-dichloro-1-fluoroethane, 1,1,1-trichloroethane, 1-chloro-3-fluoropropane, 2,3-dichloro-1,1,1-trifluoropropane, tetrachloromethane, 1-chlorobutane, 1,3-dichloro-1,1,2-trifluoropropane, 1,1-dichloro-2,2,3-trifluoropropane, 1,3,3-trichloro-1,1,2,2-tetrafluoropropane, 2-chloro-2-methylbutane, 1,2-dichloroethane, 1,1,1-trichloro-2,2,3,3-tetrafluoropropane, 1,1,3-trichloro-1,2,2,3-tetrafluoropropane, 1,3-dichloro-1,2,2-trifluoropropane, trichloroethene, 1,1-dichloropropane, 1,2-dichloro-2-fluoropropane, 2-iodopropane, dichlorobromomethane, 2-bromobutane, 2,2-difluorotetrachloroethane, 1,1,2,2-tetrachloro-1,2-difluoroethane, 1-fluorohexane, 1,3-dichloro-1,2,3-trifluoropropane, 2,3-dichloro-1-propene, 1,2-dichloropropane, 3-chloropentane, trichloroacetaldehyde, isoamyl chloride, 1,1,1-trichloro-2,2,3-trifluoropropane, 1-chloro-4-fluorobutane, 1-bromo-3-fluoropropane, 1-bromobutane, 1,1,2-trichloro-2-fluoroethane, 1-iodopropane, 1,1,3-trichloro-1,2,2-trifluoropropane, 1,1,3-trichloro-2,2,3-trifluoropropane, cis-1,3-dichloropropene, 2,2-dichlorobutane, bromotrichloromethane, 1,1,1,2-tetrachloro-2-fluoroethane, 1-bromo-2-chloroethane, 2-bromo-2-methylbutane, trans-1,3-dichloropropene, 2-fluorotoluene, 1,1,2-trichloroethane, 1,1,1-trichloro-3-fluoropropane, 3,3,3-trichloro-1-propene, 1-chloro-3,3-dimethylbutane, 1,1,1,2-tetrachloro-3,3,3-trifluoropropane, 2-bromopentane, trichloroacetyl chloride, 2,3-dichlorobutane, 1,1,3,3-tetrachloro-1,2,2-trifluoropropane, 1,1,1,3-tetrachloro-2,2,3-trifluoropropane, 1-bromo-3-methylbutane, 1,3-dichloro-trans-2-butene, 1,3-dichloropropane, tetrachloroethene, 1,2-dibromo-1-fluoroethane, 1,2,2-trichloropropane, 1,2-dichlorobutane, 1,2,2,3-tetrachloro-3,3-difluoropropane, 2,3-dichloro-2-methylbutane, 1-bromopentane, 1,2-dichloro-2-butene, 1-iodobutane, 1,2-dibromoethane, chlorobenzene, 1,1,2-trichloropropane, 1,3-dichlorobutane, pentachlorofluoroethane, 1,2-dibromopropane, 1,2,3-trichloropropene, 1-chloro-3-bromopropane, 1,1,3,3-tetrachloro-1-fluoropropane, 1,1,2,2,3-pentchloro-3,3-difluoropropane, 1,1,2,2-tetrachloroethane, 1,2-dichloropentane and tribromomethane.

Preferably, the alcohols are chosen from the group consisting of methanol, 2,2,2-trifluoroethanol, 1,1,1-trifluoro-2-propanol, ethanol, pentafluoro-1-propanol, 2-propanol, tert-butanol, 2,2-difluoroethanol, propanol, 2-allyloxyethanol, 2-butanol, 2-methyl-2-butanol, isobutanol, 2,2,3,3-tetraflouro-1-propanol, 2,2-dimethyl-1-propanol, 3-pentanol, 1-butanol, 1-methoxy2-propanol, 1-(dimethylamino)-2-propanol, 3-methyl-3-pentanol, 1-chloro-2-methyl-2-propanol, 4,4,4-trifluorobutanol, 3-fluoropropanol, 2-chloroethanol, 2-methoxy1-propanol, 1-ethoxy-2-propanol, 4-methyl-2-pentanol, 1,2-octanediol, 2-chloro-1-propanol, 2-(dimethylamino)ethanol, 3-hexanol, 2-hexanol, 2-ethoxy-1-propanol, 1-pentanol, 3,3,4,4,5,5,6,6-octafluoro-1-pentanol, 2,3-dimethylbutanol, 2-ethyl-1-butanol, 2-methyl-1-pentanol, 2-propoxyethanol, 1-propoxy-2-propanol and 2-aminophenol.

Preferably, the ketones are chosen from the group consisting of 1,1,1-trifluoro-2-propanone, propanone, butanone, 3-pentanone, 2-pentanone, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, 2-hexanone, 5-hexen-2-one and 4-methyl-2-hexanone.

Preferably, the amines are chosen from the group consisting of ethylamine, isopropylamine, ethylmethylamine, 2-amino-2-methylpropane, n-propylamine, isopropylmethylamine, diethylamine, 2-butanamine, n-methylpropylamine, 1-butylamine, diisopropylamine, 3-methyl-2-butanamine, 3-pentylamine, n-methylbutylamine, 1-methoxy-2-propanamine, 2-methoxyethanamine, 2-methoxy-1-propanamine, n-pentylamine, n-methylhydroxylamine, dipropylamine, 2-ethoxyethanamine, n-methyl-1,2-ethanediamine, pyridine, 1,2-diaminoethane, 1,2-propanediamine, 2-ethylbutylamine, n-ethylethylenediamine, 1,1-diethoxy-n,n-dimethylmethanamine, 2-methylpyridine, 4-methyl-2-hexanamine, hexylamine, cyclohexylamine, n-ethyl-2-dimethylaminoethylamine, 1,3-propanediamine, 2-heptanamine, n,n-diethylethylenediamine, 2,6-dimethylpyridine, 4-methylpyridine, n,n′-diethyl-1,2-ethanediamine and dimethylethanolamine.

Preferably, the esters are chosen from the group consisting of methyl formate, methyl acetate, isopropyl formate, ethyl acetate, n-propyl formate, isopropyl acetate, tert-butyl acetate, ethyl propionate, sec-butyl acetate, diethyl carbonate, n-butyl acetate, bromoacetic acid methyl ester and methyl hexanoate.

Preferably, the ethers are chosen from the group consisting of 2,2,2-trifluoroethyl methyl ether, 1,1,2,2-tetrafluoroethyl methyl ether, 2-methoxy-1-propene, diethyl ether, ethoxyethene, dimethoxymethane, methyl cyclopropyl ether, 2-ethoxypropane, methyl t-butyl ether, ethyl 1,1,2,2-tetrafluoroethyl ether, chloromethoxymethane, diisopropyl ether, 2-ethoxy-2-methylpropane, 2-ethoxybutane, 1-methoxy-2-methylbutane, 2,2-dimethoxypropane, 1-ethoxy-2-methylpropane, 1,2-dimethoxyethane, diethoxymethane, di-n-propyl ether, 1-ethoxybutane, 1-methoxypentane, 1,2-dimethoxypropane, isopropyl isobutyl ether, 1,1-diethoxyethane, trimethoxymethane, 1,1-dichloro-2,2-difluoroethyl methyl ether, 2,2-diethoxypropane, isobutyl tert-butyl ether, sec-butyl tert-butyl ether, 1,1-diethoxypropane, 2-methoxyethanol, 2-chloro-1,1-dimethoxyethane, methoxycyclohexane, ethoxyethanol, di-n-butyl ether, 1-ethoxyhexane, 1-methoxy-2-acetoxypropane and 1,1,1-triethoxyethane.

Preferably, the aldehydes are chosen from the group consisting of acetaldehyde, ethanedial, isobutanal, methylglyoxal, 2-methylbutanal, 2,6-dimethyl-5-heptenal and hexanal.

Preferably, the nitriles are chosen from the group consisting of acetonitrile, propionitrile, butyronitrile, valeronitrile and (methyleneamino)acetonitrile.

Preferably, the carbonate is diethyl carbonate.

Preferably, the amide is ethanethioamide.

Preferably, the thioalkyls are chosen from the group consisting of ethanethiol, dimethyl sulfide, 2-propanethiol, 4-methoxy-2-methyl-2-butanethiol, tert-butylthiol, 1-propanethiol, thiophene, 2-butanethiol, 2-methyl-1-propanethiol, diethyl sulfide, butanethiol, 3-mercapto-1,2-propanediol, tetrahydrothiophene and 1-pentanethiol.

Preferably, the heterocycles are chosen from the group consisting of furan, 1,2-epoxypropane, tetrahydrofuran, dioxane, 1,3-dioxane, piperidine, 1,3,5-trioxane, n-methylmorpholine, 2-methylpyrazine, 1-methylpiperazine, n-ethylmorpholine, 2,6-dimethylmorpholine and 3-furfural.

Said organic extracting agent may be chloroethane, 3-chloro-1,1,1,2,2,3-hexafluoropropane, 2-chloro-1,1,1,3,3,3-hexafluoropropane, 1,1,1,3,3-pentafluoropropane, ethylamine, bromofluoromethane, 1-bromo-1,2-difluoroethylene1-chloro-1,1,2,3,3,3-hexafluoropropane, 1-chloro-1,1,2,2-tetrafluoropropane, acetaldehyde, 1-chloro-1,1,2,2,3,3-hexafluoropropane, 1,1,1-trifluoro-2-propanone, 2-chloro-1,1,1,2-tetrafluoropropane, 1,1,1,2,3-pentafluoropropane, trichlorofluoromethane, 1-chloro-1,1-difluoropropane, 1,1,1-trifluoro-2-bromoethane, 1,1-dichloro-2,2,2-trifluoroethane, 1-chloro-2,2,3,3,3-pentafluoropropane, 1,2-dichloro-1,1,2-trifluoroethane, 2,2,2-trifluoroethyl methyl ether, 1,1-dichloroethylene, furan, methyl formate, isopropylamine, 1,1,2,2-tetrafluoroethyl methyl ether, 1,1,1,2,3,4,4,4-octafluorobutane, 2-methoxy-1-propene, diethyl ether, 1,2-epoxypropane, ethanethiol, 2-chloro-2-fluoropropane, ethoxyethene, 1-chloro-2,2-difluoroethane, ethylmethylamine, dimethyl sulfide, 2-chloropropane, bromoethane, dichloromethane, dimethoxymethane, 2-chloro-1,1,1,3,3-pentafluoropropane, 1-chloro-1,2,2-trifluoropropane, iodomethane, 2,2-dichloro-1,1,1,3,3-pentafluoropropane, 2-amino-2-methylpropane, methyl cyclopropyl ether, 3-chloropropene, 3-chloro-1,1,1-trifluoropropane, 1,1,1-trichloro-2,2,2-trifluoroethane, 1,2-dichloro-1,2-difluoroethane, 1,2-dichloro-1,1,2,3,3-pentafluoropropane, n-propylamine, 1,1,2-trichloro-1,2,2-trifluoroethane, 2,2-dimethylbutane, isopropylmethylamine, ethanedial, 1,2-dichloro-1,1,3,3,3-pentafluoropropane, 1-chloro-1,2,2,3-tetrafluoropropane, 1,1-dichloro-1,2,2,3,3-pentafluoropropane, 2-chloro-2-methylpropane, 3-chloro-1,1,1,3-tetrafluoropropane, 2,3-dichloro-1,1,1,2,3-pentafluoropropane, 1,1-dichloro-2,2,3,3,3-pentafluoropropane, 2-chloro-1,1,1,3-tetrafluoropropane, 2-propanethiol, 1,3-dichloro-1,1,2,3,3-pentafluoropropane, 1,2-dichloro-3,3,3-trifluoropropene, 1,3-dichloro-1,1,2,2,3-pentafluoropropane, 1,1,1,2,2,3,4,5,5,5-decafluoropentane, 2-ethoxypropane, 2,2-dichloro-1,1,1,3-tetrafluoropropane, 1-chloro-2,2-difluoropropane, methyl t-butyl ether, diethylamine, propanone, methyl acetate, 1,1-dichloroethane, ethyl 1,1,2,2-tetrafluoroethyl ether, 4-methoxy-2-methyl-2, butanethiol, 2-bromopropane, chloromethoxymethane, 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane, 1,1-dichloro-2,2-difluoroethane, 2,2-dichloro-1,1,3,3-tetrafluoropropane, difluorodiethylsilane, 2-butanamine, 2,3-dichloro-1,1,1,2-tetrafluoropropane, n-methylpropylamine, 3-methylpentane, 1,1-dichloro-1,2,2,3-tetrafluoropropane, tert-butylthiol, isobutanal, methanol, tetrahydrofuran, 1,3-dichloro-1,1,2,2-tetrafluoropropane, 1,1,1-trichloro-2,2-difluoroethane, 1,2-dichloro-1,2,3,3-tetrafluoropropane, 1-propanethiol, chlorobromomethane, 2-chlorobutane, isopropyl formate, diisopropyl ether, 1,3-dichloro-1,1,3,3-tetrafluoropropane, hexane, 1,3-dichloro-1,2,2,3-tetrafluoropropane, 1,2-dichloro-1,1,2,3-tetrafluoropropane, 3-bromopropene, 2,3-dichloro-1,1,1,3-tetrafluoropropane, 1,1-dichloro-2-fluoroethane, 1-bromopropane, 1,1-difluoro-1,2,2-trichloroethane, 1,1,2-trichloro-1,2-difluoroethane, methylglyoxal, iodoethane, 2-ethoxy-2-methylpropane, 2-bromo-2-methylpropane, 1,2-dichloro-1-fluoroethane, 1,1,1-trichloroethane, 2,2,2-trifluoroethanol, 1-chloro-3-fluoropropane, 1,1,1-trifluoro-2-propanol, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, 1-butylamine, 1-chlorobutane, ethanol, butanone, 2,4-dimethylpentane, cyclohexane, n-propyl formate, 2-ethoxybutane, acetonitrile, pentafluoro-1-propanol, 2-propanol, tert-butanol, 1,3-dichloro-1,1,2-trifluoropropane, 1-methoxy-2-methylbutane, 1,1-dichloro-2,2,3-trifluoropropane, cyclohexene, 2,2-dimethoxypropane, 1,3,3-trichloro-1,1,2,2-tetrafluoropropane, 2-chloro-2-methylbutane, 1,2-dichloroethane, 1-ethoxy-2-methylpropane, diisopropylamine, thiophene, 2-butanethiol, 1,1,1-trichloro-2,2,3,3-tetrafluoropropane, 1,2-dimethoxyethane, 3-methyl-2-butanamine, 1,1,3-trichloro-1,2,2,3-tetrafluoropropane, 1,3-dichloro-1,2,2-trifluoropropane, diethoxymethane, 1,1-dichloropropane, 2-methyl-1-propanethiol, 1,2-dichloro-2-fluoropropane, isopropyl acetate, 2-iodopropane, di-n-propyl ether, 3-pentylamine, n-methylbutylamine, 2-bromobutane, 2,2-difluorotetrachloroethane, diethyl sulfide, 1-ethoxybutane, 1,1,2,2-tetrachloro-1,2-difluoroethane, 1-fluorohexane, 1-methoxy-2-propanamine, 1,3-dichloro-1,2,3-trifluoropropane, 2,3-dichloro-1-propene, 2-methoxyethanamine, 2,2-difluoroethanol, 2-methylbutanal, 1,2-dichloropropane, propanol, tert-butyl acetate, propionitrile, 3-chloropentane, trichloroacetaldehyde, 2-allyloxyethanol, butanethiol, isoamyl chloride, 1-methoxypentane, ethyl propionate, 2-butanol, 1,2-dimethoxypropane, isopropyl isobutyl ether, 1,1,1-trichloro-2,2,3-trifluoropropane, methylcyclohexane, 1-chloro-4-fluorobutane, 1-bromo-3-fluoropropane, 2,4,4-trimethyl-1-pentene, dioxane, 1-bromobutane, 3-pentanone, 1,1,2-trichloro-2-fluoroethane, 1,1-diethoxyethane, 2-pentanone, 2-methyl-2-butanol, 1-iodopropane, 2-methoxy-1-propanamine, 1,1,3-trichloro-1,2,2-trifluoropropane, 1,1,3-trichloro-2,2,3-trifluoropropane, trimethoxymethane, cis-1,3-dichloropropene, 2,2-dichlorobutane, n-pentylamine, 1,1-dichloro-2,2-difluoroethyl methyl ether, 2,2,4-trimethyl-2-pentene, 1,1,1,2-tetrachloro-2-fluoroethane, 1,3-dioxane, 3,3-dimethyl-2, butanone, piperidine, 1-bromo-2-chloroethane, isobutanol, 2-bromo-2-methylbutane, dipropylamine, 2,2,3,3-tetraflouro-1-propanol, 2-ethoxyethanamine, triethylfluorosilane, 1-methylcyclohexene, toluene, trans-1,3-dichloropropene, sec-butyl acetate, 2-fluorotoluene, 2,2-dimethyl-1-propanol, 1,1,1-trichloro-3-fluoropropane, n-methyl-1,2-ethanediamine, 2,2-diethoxypropane, 1,3,5-trioxane, 3,3,3-trichloro-1-propene, 1-chloro-3,3-dimethylbutane, pyridine, 2,3-dimethylhexane, 1,1,1,2-tetrachloro-3,3,3-trifluoropropane, n-methylmorpholine, 3-pentanol, 4-methyl-2-pentanone, 1,2-diaminoethane, isobutyl tert-butyl ether, 2-bromopentane, butyronitrile, 1-butanol, 2,3-dichlorobutane, sec-butyl tert-butyl ether, 1-methoxy-2-propanol, 1,1,3,3-tetrachloro-1,2,2-trifluoropropane, 1,2-propanediamine, 2,6-dimethyl-5-heptenal, perfluorobutanoic acid, 1,1,1,3-tetrachloro-2,2,3-trifluoropropane, 1-bromo-3-methylbutane, 1,3-dichloro-trans-2-butene, 1,3-dichloropropane,1-(dimethylamino)-2-propanol, tetrahydrothiophene, 3-methyl-3-pentanol, 1,2-dibromo-1-fluoroethane, 1,1-diethoxypropane, 1,2,2-trichloropropane, 1-chloro-2-methyl-2, propanol, 2-methoxyethanol, 1,2-dichlorobutane, 4,4,4-trifluorobutanol, 2-ethylbutylamine, octane, diethyl carbonate, n-butyl acetate, 1-pentanethiol, 1,2,2,3-tetrachloro-3,3-difluoropropane, 2-chloro-1,1-dimethoxyethane, 2-hexanone, n-ethylethylenediamine, 3-fluoropropanol, 5-hexen-2-one, 2,3-dichloro-2-methylbutane, 1,1-diethoxy-n,n-dimethylmethanamine, 2-methylpyridine, 1-bromopentane, 2-methoxy-1-propanol, 1,2-dichloro-2-butene, 1-iodobutane, 1-ethoxy-2-propanol, hexanal, 4-methyl-2-pentanol, 1,2-dibromoethane, chlorobenzene, ethylcyclohexane, bromoacetic acid methyl ester, 1,1,2-trichloropropane, 1,2-octanediol, 4-methyl-2-hexanamine, hexylamine, 2-chloro-1-propanol, methoxycyclohexane, 2-(dimethylamino)ethanol, 1,3-dichlorobutane, cyclohexylamine, n-ethyl-2-dimethylaminoethylamine, ethoxyethanol, 3-hexanol, 2-hexanol, ethylbenzene, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-pentanol, 1-methylpiperazine, n-ethylmorpholine, 1,4-dimethylbenzene, 1,3-dimethylbenzene, 1,3-propanediamine, di-n-butyl ether, 3,3,4,4,5,5,6,6-octafluoro-1-pentanol, valeronitrile, (methyleneamino)acetonitrile, 1,2-dibromopropane, 2-heptanamine, 1,2,3-trimethylcyclohexane, 2,3-dimethylbutanol, 1-ethoxyhexane, 1-chloro-3-bromopropane, 3-furfural, n,n-diethylethylenediamine, 2,6-dimethylpyridine, 1,1,3,3-tetrachloro-1-fluoropropane, 4-methyl-2-hexanone, 1,2-dimethylbenzene, 1,1,2,2,3-pentchloro-3,3-difluoropropane, 1-methoxy-2-acetoxypropane, 1,1,1-triethoxyethane, styrene, 4-methylpyridine, n,n′-diethyl-1,2-ethanediamine, 2,6-dimethylmorpholine, 2-ethyl-1-butanol, 1,2-dichloropentane, 2-methyl-1-pentanol, methyl hexanoate, 2-propoxyethanol, dimethylethanolamine or 1-propoxy-2-propanol.

Advantageously, said organic extracting agent may be chloroethane, 1,1,1,3,3-pentafluoropropane, bromofluoromethane, 1-bromo-1,2-difluoroethylene, 1-chloro-1,1,2,2-tetrafluoropropane, acetaldehyde, 1,1,1-trifluoro-2-propanone, 2-chloro-1,1,1,2-tetrafluoropropane, 1,1,1,2,3-pentafluoropropane, 1-chloro-1,1-difluoropropane, 1,1,1-trifluoro-2-bromoethane, 1,1-dichloro-2,2,2-trifluoroethane, 1-chloro-2,2,3,3,3-pentafluoropropane, 1,2-dichloro-1,1,2-trifluoroethane, 2,2,2-trifluoroethylmethylether, furan, methyl formate, isopropylamine, 1,1,2,2-tetrafluoroethyl methyl ether, 2-methoxy-1-propene, diethyl ether, 1,2-epoxypropane, ethanethiol, 2-chloro-2-fluoropropane, ethoxyethene, 1-chloro-2,2-difluoroethane, ethylmethylamine, dimethyl sulfide, 2-chloropropane, bromoethane, dimethoxymethane, 2-chloro-1,1,1,3,3-pentafluoropropane, 1-chloro-1,2,2-trifluoropropane, 2,2-dichloro-1,1,1,3,3-pentafluoropropane, 2-amino-2-methylpropane, methyl cyclopropyl ether, 3-chloropropene, 3-chloro-1,1,1-trifluoropropane, 1,1,1-trichloro-2,2,2-trifluoroethane, 1,2-dichloro-1,2-difluoroethane, 1,2-dichloro-1,1,2,3,3-pentafluoropropane, 1,1,2-trichloro-1,2,2-trifluoroethane, isopropylmethylamine, ethanedial, 1,2-dichloro-1,1,3,3,3-pentafluoropropane, 1-chloro-1,2,2,3-tetrafluoropropane, 1,1-dichloro-1,2,2,3,3-pentafluoropropane, 2-chloro-2-methylpropane, 3-chloro-1,1,1,3-tetrafluoropropane, 2,3-dichloro-1,1,1,2,3-pentafluoropropane, 1,1-dichloro-2,2,3,3,3-pentafluoropropane, 2-chloro-1,1,1,3-tetrafluoropropane, 2-propanethiol, 1,2-dichloro-3,3,3-trifluoropropene, 2-ethoxypropane, 2,2-dichloro-1,1,1,3-tetrafluoropropane, 1-chloro-2,2-difluoropropane, methyl t-butyl ether, diethylamine, propanone, methyl acetate, ethyl 1,1,2,2-tetrafluoroethyl ether, 4-methoxy-2-methyl-2-butanethiol, 2-bromopropane, 1,1-dichloro-2,2-difluoroethane, 2,2-dichloro-1,1,3,3-tetrafluoropropane, difluorodiethylsilane, 2,3-dichloro-1,1,1,2-tetrafluoropropane, 1,1-dichloro-1,2,2,3-tetrafluoropropane, tert-butylthiol, isobutanal, tetrahydrofuran, 1,3-dichloro-1,1,2,2-tetrafluoropropane, 1,1,1-trichloro-2,2-difluoroethane, 1,2-dichloro-1,2,3,3-tetrafluoropropane, 1-propanethiol, 2-chlorobutane, isopropyl formate, diisopropyl ether, 1,3-dichloro-1,2,2,3-tetrafluoropropane, 1,2-dichloro-1,1,2,3-tetrafluoropropane, 2,3-dichloro-1,1,1,3-tetrafluoropropane, 1-bromopropane, 1,1-difluoro-1,2,2-trichloroethane, 1,1,2-trichloro-1,2-difluoroethane, methylglyoxal, 2-ethoxy-2-methylpropane, 2-bromo-2-methylpropane, 1-chloro-3-fluoropropane, 1,1,1-trifluoro-2-propanol, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, 1-chlorobutane, butanone, n-propyl formate, 2-ethoxybutane, pentafluoro-1-propanol, tert-butanol, 1,3-dichloro-1,1,2-trifluoropropane, 1-methoxy-2-methylbutane, 1,1-dichloro-2,2,3-trifluoropropane, cyclohexene, 2,2-dimethoxypropane, 1,3,3-trichloro-1,1,2,2-tetrafluoropropane, 2-chloro-2-methylbutane, 1-ethoxy-2-methylpropane, diisopropylamine, 2-butanethiol, 1,1,1-trichloro-2,2,3,3-tetrafluoropropane, 1,2-dimethoxyethane, 1,1,3-trichloro-1,2,2,3-tetrafluoropropane, 1,3-dichloro-1,2,2-trifluoropropane, diethoxymethane, 2-methyl-1-propanethiol, isopropyl acetate, 2-iodopropane, di-n-propyl ether, 2-bromobutane, diethyl sulfide, 1-ethoxybutane, 1-fluorohexane, 1-methoxy-2-propanamine, 1,3-dichloro-1,2,3-trifluoropropane, 2-methoxyethanamine, 2-methylbutanal, tert-butyl acetate, propionitrile, 3-chloropentane, 2-allyloxyethanol, butanethiol, isoamyl chloride, 1-methoxypentane, ethyl propionate, 2-butanol, 1,2-dimethoxypropane, isopropyl isobutyl ether, 1,1,1-trichloro-2,2,3-trifluoropropane, 1-chloro-4-fluorobutane, 1-bromo-3-fluoropropane, 2,4,4-trimethyl-1-pentene, dioxane, 1-bromobutane, 3-pentanone, 1,1-diethoxyethane, 2-pentanone, 2-methyl-2-butanol, 2-methoxy-1-propanamine, 1,1,3-trichloro-1,2,2-trifluoropropane, 1,1,3-trichloro-2,2,3-trifluoropropane, trimethoxymethane, 1,1-dichloro-2,2-difluoroethyl methyl ether, 2,2,4-trimethyl-2-pentene, 1,3-dioxane, 3,3-dimethyl-2-butanone, piperidine, 2-bromo-2-methylbutane, dipropylamine, 2,2,3,3-tetraflouro-1-propanol, 2-ethoxyethanamine, triethylfluorosilane, 1-methylcyclohexene, toluene, sec-butyl acetate, 2-fluorotoluene, 2,2-dimethyl-1-propanol, n-methyl-1,2-ethanediamine, 2,2-diethoxypropane, 1,3,5-trioxane, 1-chloro-3,3-dimethylbutane, pyridine, 1,1,1,2-tetrachloro-3,3,3-trifluoropropane, n-methylmorpholine, 3-pentanol, 4-methyl-2-pentanone, 1,2-diaminoethane, isobutyl tert-butyl ether, 2-bromopentane, butyronitrile, 1-butanol, sec-butyl tert-butyl ether, 1-methoxy-2-propanol, 1,1,3,3-tetrachloro-1,2,2-trifluoropropane, 1,2-propanediamine, 2,6-dimethyl-5-heptenal, 1,1,1,3-tetrachloro-2,2,3-trifluoropropane, 1-bromo-3-methylbutane, 1-(dimethylamino)-2-propanol, tetrahydrothiophene, 3-methyl-3-pentanol, 1,1-diethoxypropane, 2-methoxyethanol, 4,4,4-trifluorobutanol, diethyl carbonate, n-butyl acetate, 1-pentanethiol, 2-chloro-1,1-dimethoxyethane, 2-hexanone, n-ethylethylenediamine, 5-hexen-2-one, 1,1-diethoxy-n,n-dimethylmethanamine, 2-methylpyridine, 1-bromopentane, 2-methoxy1-propanol, 1-ethoxy-2-propanol, hexanal, 4-methyl-2-pentanol, 1,2-octanediol, methoxycyclohexane, 2-(dimethylamino)ethanol, cyclohexylamine, n-ethyl-2-dimethylaminoethylamine, ethoxyethanol, 3-hexanol, 2-hexanol, ethylbenzene, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-pentanol, 1-methylpiperazine, n-ethylmorpholine, 1,4-dimethylbenzene, 1,3-dimethylbenzene, 1,3-propanediamine, di-n-butyl ether, 3,3,4,4,5,5,6,6-octafluoro-1-pentanol, valeronitrile, (methyleneamino)acetonitrile, 2,3-dimethylbutanol, 1-ethoxyhexane, 3-furfural, 2,6-dimethylpyridine, 4-methyl-2-hexa none, 1,2-dimethylbenzene, 1-methoxy-2-acetoxypropane, 1,1,1-triethoxyethane, styrene, 4-methylpyridine, n,n′-diethyl-1,2-ethanediamine, 2,6-dimethylmorpholine, 2-ethyl-1-butanol, 2-methyl-1-pentanol, methyl hexanoate, 2-propoxyethanol, dimethylethanolamine or 1-propoxy-2-propanol.

Preferably, said organic extracting agent may be acetaldehyde, methyl formate, 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, 1-chloro-1,2,2-trifluoropropane, 3-chloro-1,1,1-trifluoropropane, ethanedial, 2-chloro-1,1,1,3-tetrafluoropropane, propanone, methyl acetate, 4-methoxy-2-methyl-2-butanethiol, difluorodiethylsilane, isobutanal, isopropyl formate, methylglyoxal, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, butanone, n-propyl formate, 1,3-dichloro-1,1,2-trifluoropropane, 1,1-dichloro-2,2,3-trifluoropropane, 1,2-dimethoxyethane, 1,3-dichloro-1,2,2-trifluoropropane, isopropyl acetate, diethyl sulfide, 1,3-dichloro-1,2,3-trifluoropropane, 2-methylbutanal, 2-allyloxyethanol, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, pyridine, n-methylmorpholine, 4-methyl-2-pentanone, butyronitrile, 1-methoxy-2-propanol, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 2-methoxy-1-propanol, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-methylpiperazine, n-ethylmorpholine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate, 2-propoxyethanol or 1-propoxy-2-propanol.

In particular, said organic extracting agent may be 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, n-propyl formate, 1,2-dimethoxyethane, isopropyl acetate, 2-methylbutanal, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 1-methylpiperazine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate or 1-propoxy-2-propanol.

The organic extracting agent to be used may be chosen as a function of the compounds present in said first composition. Thus, the organic extracting agent may be chosen as a function of the separation factor and of the absorption capacity established for a particular composition. Besides these two criteria, the choice of the organic extracting agent may be optionally based on other commercial or environmental criteria, for instance the cost of the organic extracting agent, its availability on the market, and its toxicity or flammability properties. Furthermore, according to a particular embodiment, in order to optimize the functioning of the distillation columns used in the steps b) and c) of the present process for purifying 2,3,3,3-tetrafluoro-1-propene, the boiling point of the organic extracting agent may be from 10° C. to 200° C., advantageously from 10° C. to 190° C., preferably from 10° C. to 180° C., in particular from 10° C. to 170° C., preferentially from 10° C. to 160° C. and more preferentially from 10° C. to 150° C.

According to a preferred embodiment, said organic extracting agent has a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which

-   -   γ_(1,S) represents the activity coefficient of         2,3,3,3-tetrafluoro-1-propene in said organic extracting agent         at infinite dilution;     -   P1 represents the saturating vapor pressure of         2,3,3,3-tetrafluoro-1-propene;     -   γ_(2,S) represents the activity coefficient of one of the         compounds consisting of chloromethane (40), 1,1-difluoroethane         (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane         (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf) in said organic extracting agent         at infinite dilution; advantageously, the activity coefficient         of 3,3,3-trifluoropropene (1243zf) or         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E);     -   P2 represents the saturating vapor pressure of one of the         compounds consisting of chloromethane (40), 1,1-difluoroethane         (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane         (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf); advantageously, the saturating         vapor pressure of 3,3,3-trifluoropropene (1243zf) or         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E).

Advantageously, the separation factor S_(1,2) is greater than or equal to 1.2, preferably greater than or equal to 1.4, more preferentially greater than or equal to 1.6, in particular greater than or equal to 1.8, more particularly greater than or equal to 2.0.

According to a preferred embodiment, said organic extracting agent has an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of one of the compounds consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution; advantageously, the activity coefficient of 3,3,3-trifluoropropene (1243zf) or trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E).

Advantageously, the absorption capacity C_(2,S) is greater than or equal to 0.40, preferably greater than or equal to 0.60, more preferentially greater than or equal to 0.80, in particular greater than or equal to 1.0.

According to a preferred embodiment, said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.1, advantageously greater than or equal to 1.2, preferably greater than or equal to 1.4, more preferentially greater than or equal to 1.6 and in particular greater than or equal to 1.8; and an absorption capacity C_(2,S) of greater than or equal to 0.20, advantageously greater than or equal to 0.40, preferably greater than or equal to 0.60, more preferentially greater than or equal to 0.80 and in particular greater than or equal to 1.0.

Said first composition may be an azeotropic or quasi-azeotropic composition comprising 2,3,3,3-tetrafluoro-1-propene and at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf). Advantageously, said first composition may be an azeotropic or quasi-azeotropic composition comprising 2,3,3,3-tetrafluoro-1-propene and at least two, at least three, at least four, at least five, at least six or all of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf). Preferably, said first composition may be an azeotropic or quasi-azeotropic composition comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

Depending on the compound(s) to be removed in said first composition, said separation factor and said absorption capacity may be calculated for a particular binary couple consisting of 2,3,3,3-tetrafluoro-1-propene and one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf). Thus, to select said organic extracting agent that is suitable for use in the extractive distillation step b), the separation factor and the absorption capacity may be calculated, for example, for a 2,3,3,3-tetrafluoro-1-propene and 3,3,3-trifluoropropene (1243zf) binary couple if said first composition comprises these two compounds. The separation factor S_(1,2) makes it possible to determine the capacity of an organic extracting agent to separate two or more compounds. The absorption capacity C_(2,S) makes it possible to determine the amount of solvent to be used to obtain separation between the compounds under consideration. In addition, if it is desired to optimize the separation of a first composition, the separation factor and the absorption capacity may be calculated for several binary couples, and the organic extracting agent is thus selected on the basis of the values obtained for all or some of the binary couples under consideration.

In particular, said first composition may thus be an azeotropic or quasi-azeotropic composition comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf) and trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E). The content of each of the compounds in this particular composition is as expressed above with reference to the individual contents of each of the compounds. Thus, the second composition may comprise 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and said organic extracting agent.

Said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene, γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution and P2 represents the saturating vapor pressure of 3,3,3-trifluoropropene (1243zf); advantageously, said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.2, preferably greater than or equal to 1.4, more preferentially greater than or equal to 1.6, in particular greater than or equal to 1.8 and more particularly greater than or equal to 2.0; and said organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene, γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution and P2 represents the saturating vapor pressure of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E); advantageously, said organic extracting agent may have a separation factor of greater than or equal to 1.2, preferably greater than or equal to 1.4, more preferentially greater than or equal to 1.6, in particular greater than or equal to 1.8, more particularly greater than or equal to 2.0.

The separation factor of said organic extracting agent may be different depending on the binary couple under consideration. Thus, the organic extracting agent may be chosen so as to have a separation factor of greater than or equal to 1.4 on the basis of the (1234yf/1243zf) binary couple and may have a separation factor of greater than or equal to 1.6 on the basis of the (1234yf/1234zeE) binary couple. This is likewise the case for the absorption capacity.

Thus, said organic extracting agent may have an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution; advantageously, the absorption capacity C_(2,S) may be greater than or equal to 0.40, preferably greater than or equal to 0.60, more preferentially greater than or equal to 0.80 and in particular greater than or equal to 1.0; and said organic extracting agent may have an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution; advantageously, the absorption capacity C_(2,S) is greater than or equal to 0.40, preferably greater than or equal to 0.60, more preferentially greater than or equal to 0.80, in particular greater than or equal to 1.0.

Thus, said organic extracting agent may have:

-   -   a separation factor S_(1,2) of greater than or equal to 1.1,         said separation factor being calculated by the formula         S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the         activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said         organic extracting agent at infinite dilution, P1 represents the         saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene,         γ_(2,S) represents the activity coefficient of         3,3,3-trifluoropropene (1243zf) in said organic extracting agent         at infinite dilution and P2 represents the saturating vapor         pressure of 3,3,3-trifluoropropene (1243zf); advantageously,         said organic extracting agent may have a separation factor of         greater than or equal to 1.2, preferably greater than or equal         to 1.4, more preferentially greater than or equal to 1.6, in         particular greater than or equal to 1.8 and more particularly         greater than or equal to 2.0;     -   an absorption capacity C_(2,S) of greater than or equal to 0.20,         said absorption capacity being calculated by the formula         C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity         coefficient of 3,3,3-trifluoropropene (1243zf) in said organic         extracting agent at infinite dilution; advantageously, the         absorption capacity C_(2,S) may be greater than or equal to         0.40, preferably greater than or equal to 0.60, more         preferentially greater than or equal to 0.80, in particular         greater than or equal to 1.0;     -   a separation factor S_(1,2) of greater than or equal to 1.1,         said separation factor being calculated by the formula         S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which γ_(1,S) represents the         activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said         organic extracting agent at infinite dilution, P1 represents the         saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene,         γ_(2,S) represents the activity coefficient of         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic         extracting agent at infinite dilution and P2 represents the         saturating vapor pressure of trans-1,3,3,3-tetrafluoro-1-propene         (1234ze-E); advantageously, said organic extracting agent may         have a separation factor of greater than or equal to 1.2,         preferably greater than or equal to 1.4, more preferentially         greater than or equal to 1.6, in particular greater than or         equal to 1.8 and more particularly greater than or equal to 2.0;         and     -   an absorption capacity C_(2,S) of greater than or equal to 0.20,         said absorption capacity being calculated by the formula         C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity         coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in         said organic extracting agent at infinite dilution;         advantageously, the absorption capacity C_(2,S) may be greater         than or equal to 0.40, preferably greater than or equal to 0.60,         more preferentially greater than or equal to 0.80, in particular         greater than or equal to 1.0.

For example, said organic extracting agent may be chosen so as to have a separation factor of greater than or equal to 1.2 and so as to have an absorption capacity of greater than or equal to 0.4 for the two binary couples 2,3,3,3-tetrafluoro-1-propene/trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and 2,3,3,3-tetrafluoro-1-propene/3,3,3-trifluoropropene (1243zf). Thus, said organic extracting agent may be chosen from the group consisting of chloroethane, 1,1,1,3,3-pentafluoropropane, bromofluoromethane, 1-bromo-1,2-difluoroethylene, 1-chloro-1,1,2,2-tetrafluoropropane, acetaldehyde, 1,1,1-trifluoro-2-propanone, 2-chloro-1,1,1,2-tetrafluoropropane, 1,1,1,2,3-pentafluoropropane, 1-chloro-1,1-difluoropropane, 1,1,1-trifluoro-2-bromoethane, 1,1-dichloro-2,2,2-trifluoroethane, 1-chloro-2,2,3,3,3-pentafluoropropane, 1,2-dichloro-1,1,2-trifluoroethane, 2,2,2-trifluoroethyl methyl ether, furan, methyl formate, isopropylamine, 1,1,2,2-tetrafluoroethyl methyl ether, 2-methoxy-1-propene, diethyl ether, 1,2-epoxypropane, ethanethiol, 2-chloro-2-fluoropropane, ethoxyethene, 1-chloro-2,2-difluoroethane, ethyl methyl amine, dimethyl sulfide, 2-chloropropane, bromoethane, dimethoxymethane, 2-chloro-1,1,1,3,3-pentafluoropropane, 1-chloro-1,2,2-trifluoropropane, 2,2-dichloro-1,1,1,3,3-pentafluoropropane, 2-amino-2-methylpropane, methyl cyclopropyl ether, 3-chloropropene, 3-chloro-1,1,1-trifluoropropane, 1,1,1-trichloro-2,2,2-trifluoroethane, 1,2-dichloro-1,2-difluoroethane, 1,2-dichloro-1,1,2,3,3-pentafluoropropane, 1,1,2-trichloro-1,2,2-trifluoroethane, isopropylmethylamine, ethanedial, 1,2-dichloro-1,1,3,3,3-pentafluoropropane, 1-chloro-1,2,2,3-tetrafluoropropane, 1,1-dichloro-1,2,2,3,3-pentafluoropropane, 2-chloro-2-methylpropane, 3-chloro-1,1,1,3-tetrafluoropropane, 2,3-dichloro-1,1,1,2,3-pentafluoropropane, 1,1-dichloro-2,2,3,3,3-pentafluoropropane, 2-chloro-1,1,1,3-tetrafluoropropane, 2-propanethiol, 1,2-dichloro-3,3,3-trifluoropropene, 2-ethoxypropane, 2,2-dichloro-1,1,1,3-tetrafluoropropane, 1-chloro-2,2-difluoropropane, methyl t-butyl ether, diethylamine, propanone, methyl acetate, ethyl 1,1,2,2-tetrafluoroethyl ether, 4-methoxy-2-methyl-2-butanethiol, 2-bromopropane, 1,1-dichloro-2,2-difluoroethane, 2,2-dichloro-1,1,3,3-tetrafluoropropane, difluorodiethylsilane, 2,3-dichloro-1,1,1,2-tetrafluoropropane, 1,1-dichloro-1,2,2,3-tetrafluoropropane, tert-butylthiol, isobutanal, tetrahydrofuran, 1,3-dichloro-1,1,2,2-tetrafluoropropane, 1,1,1-trichloro-2,2-difluoroethane, 1,2-dichloro-1,2,3,3-tetrafluoropropane, 1-propanethiol, 2-chlorobutane, isopropyl formate, diisopropyl ether, 1,3-dichloro-1,2,2,3-tetrafluoropropane, 1,2-dichloro-1,1,2,3-tetrafluoropropane, 2,3-dichloro-1,1,1,3-tetrafluoropropane, 1-bromopropane, 1,1-difluoro-1,2,2-trichloroethane, 1,1,2-trichloro-1,2-difluoroethane, methylglyoxal, 2-ethoxy-2-methylpropane, 2-bromo-2-methylpropane, 1-chloro-3-fluoropropane, 1,1,1-trifluoro-2-propanol, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, 1-chlorobutane, butanone, n-propyl formate, 2-ethoxybutane, pentafluoro-1-propanol, tert-butanol, 1,3-dichloro-1,1,2-trifluoropropane, 1-methoxy-2-methylbutane, 1,1-dichloro-2,2,3-trifluoropropane, cyclohexene, 2,2-dimethoxypropane, 1,3,3-trichloro-1,1,2,2-tetrafluoropropane, 2-chloro-2-methylbutane, 1-ethoxy-2-methylpropane, diisopropylamine, 2-butanethiol, 1,1,1-trichloro-2,2,3,3-tetrafluoropropane, 1,2-dimethoxyethane, 1,1,3-trichloro-1,2,2,3-tetrafluoropropane, 1,3-dichloro-1,2,2-trifluoropropane, diethoxymethane, 2-methyl-1-propanethiol, isopropyl acetate, 2-iodopropane, di-n-propyl ether, 2-bromobutane, diethyl sulfide, 1-ethoxybutane, 1-fluorohexane, 1-methoxy-2-propanamine, 1,3-dichloro-1,2,3-trifluoropropane, 2-methoxyethanamine, 2-methylbutanal, tert-butyl acetate, propionitrile, 3-chloropentane, 2-allyloxyethanol, butanethiol, isoamyl chloride, 1-methoxypentane, ethyl propionate, 2-butanol, 1,2-dimethoxypropane, isopropyl isobutyl ether, 1,1,1-trichloro-2,2,3-trifluoropropane, 1-chloro-4-fluorobutane, 1-bromo-3-fluoropropane, 2,4,4-trimethyl-1-pentene, dioxane, 1-bromobutane, 3-pentanone, 1,1-diethoxyethane, 2-pentanone, 2-methyl-2-butanol, 2-methoxy-1propanamine, 1,1,3-trichloro-1,2,2-trifluoropropane, 1,1,3-trichloro-2,2,3-trifluoropropane, trimethoxymethane, 1,1-dichloro-2,2-difluoroethyl methyl ether, 2,2,4-trimethyl-2-pentene, 1,3-dioxane, 3,3-dimethyl-2-butanone, piperidine, 2-bromo-2-methylbutane, dipropylamine, 2,2,3,3-tetraflouro-1-propanol, 2-ethoxyethanamine, triethylfluorosilane, 1-methylcyclohexene, toluene, sec-butyl acetate, 2-fluorotoluene, 2,2-dimethyl-1-propanol, n-methyl-1,2-ethanediamine, 2,2-diethoxypropane, 1,3,5-trioxane, 1-chloro-3,3-dimethylbutane, pyridine, 1,1,1,2-tetrachloro-3,3,3-trifluoropropane, n-methylmorpholine, 3-pentanol, 4-methyl-2-pentanone, 1,2-diaminoethane, isobutyl tert-butyl ether, 2-bromopentane, butyronitrile, 1-butanol, sec-butyl tert-butyl ether, 1-methoxy-2-propanol, 1,1,3,3-tetrachloro-1,2,2-trifluoropropane, 1,2-propanediamine, 2,6-dimethyl-5-heptenal, 1,1,1,3-tetrachloro-2,2,3-trifluoropropane, 1-bromo-3-methylbutane, 1-(dimethylamino)-2-propanol, tetrahydrothiophene, 3-methyl-3-pentanol, 1,1-diethoxypropane, 2-methoxyethanol, 4,4,4-trifluorobutanol, diethyl carbonate, n-butyl acetate, 1-pentanethiol, 2-chloro-1,1-dimethoxyethane, 2-hexanone, n-ethylethylenediamine, 5-hexen-2-one, 1,1-diethoxy-n,n-dimethylmethanamine, 2-methylpyridine, 1-bromopentane, 2-methoxy-1-propanol, 1-ethoxy-2-propanol, hexanal, 4-methyl-2-pentanol, 1,2-octanediol, methoxycyclohexane, 2-(dimethylamino)ethanol, cyclohexylamine, n-ethyl-2-dimethylaminoethylamine, ethoxyethanol, 3-hexanol, 2-hexanol, ethylbenzene, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-pentanol, 1-methylpiperazine, n-ethylmorpholine, 1,4-dimethylbenzene, 1,3-dimethylbenzene, 1,3-propanediamine, di-n-butyl ether, 3,3,4,4,5,5,6,6-octafluoro-1-pentanol, valeronitrile, (methyleneamino)acetonitrile, 2,3-dimethylbutanol, 1-ethoxyhexane, 3-furfural, 2,6-dimethylpyridine, 4-methyl-2-hexa none, 1,2-dimethylbenzene, 1-methoxy-2-acetoxypropane, 1,1,1-triethoxyethane, styrene, 4-methylpyridine, n,n′-diethyl-1,2-ethanediamine, 2,6-dimethylmorpholine, 2-ethyl-1-butanol, 2-methyl-1-pentanol, methyl hexanoate, 2-propoxyethanol, dimethylethanolamine and 1-propoxy-2-propanol.

Said organic extracting agent may also be chosen so as to have a separation factor of greater than or equal to 1.4 and so as to have an absorption capacity of greater than or equal to 0.6 for the two binary couples 2,3,3,3-tetrafluoro-1-propene/trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and 2,3,3,3-tetrafluoro-1-propene/3,3,3-trifluoropropene (1243zf). Thus, said organic extracting agent may be chosen from the group consisting of acetaldehyde, methyl formate, 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, 1-chloro-1,2,2-trifluoropropane, 3-chloro-1,1,1-trifluoropropane, ethanedial, 2-chloro-1,1,1,3-tetrafluoropropane, propanone, methyl acetate, 4-methoxy-2-methyl-2-butanethiol, difluorodiethylsilane, isobutanal, isopropyl formate, methylglyoxal, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, butanone, n-propyl formate, 1,3-dichloro-1,1,2-trifluoropropane, 1,1-dichloro-2,2,3-trifluoropropane, 1,2-dimethoxyethane, 1,3-dichloro-1,2,2-trifluoropropane, isopropyl acetate, diethyl sulfide, 1,3-dichloro-1,2,3-trifluoropropane, 2-methylbutanal, 2-allyloxyethanol, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, pyridine, n-methylmorpholine, 4-methyl-2-pentanone, butyronitrile, 1-methoxy-2-propanol, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 2-methoxy-1-propanol, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-methylpiperazine, n-ethyl-morpholine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate, 2-propoxyethanol and 1-propoxy-2-propanol.

In particular, said chosen organic extracting agent may have a separation factor S_(1,2) of greater than or equal to 1.4 and absorption capacity C_(2,S) of greater than or equal to 0.8 when they are calculated for the 1234 yf/1243zf binary couple; and a separation factor S_(1,2) of greater than or equal to 1.6 and absorption capacity C_(2,S) of greater than or equal to 0.8 when they are calculated for the 1234 yf/1234zeE binary couple. In this case, said organic extracting agent may be chosen from the group consisting of 2-methoxy-1-propene,1,2-epoxypropane, ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, n-propyl formate, 1,2-dimethoxyethane, isopropyl acetate, 2-methylbutanal, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 1-methylpiperazine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate and 1-propoxy-2-propanol. Preferably, said organic extracting agent may be chosen from the group consisting of ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, 1,2-dimethoxyethane, isopropyl acetate, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butyl acetate, 1-ethoxy-2-propanol and hexanal. In particular, said organic extracting agent may be chosen from the group consisting of dimethoxymethane, butanone, isopropyl acetate, dioxane, trimethoxymethane, 1,3-dioxane, n-butyl acetate, 1-ethoxy-2-propanol and hexanal. More particularly, said organic extracting agent may be chosen from the group consisting of dimethoxymethane, isopropyl acetate, dioxane, trimethoxymethane, 1,3-dioxane, n-butyl acetate, 1-ethoxy-2-propanol and hexanal.

According to a preferred embodiment, said third composition may be subjected to a distillation to separate, on the one hand, the organic extracting agent and, on the other hand, said at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf). Advantageously, said third composition may be subjected to distillation to separate, on the one hand, the organic extracting agent and, on the other hand, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

According to a particular embodiment, the stream comprising 2,3,3,3-tetrafluoropropene separated out in step b) of the present process is subsequently purified or liquefied and stored. According to this embodiment, traces of organic extracting agent may be present in the stream comprising 2,3,3,3-tetrafluoropropene. The traces of organic extracting agent in said stream are less than 10 ppm, preferably less than 1 ppm, in particular less than 500 ppb and more particularly less than 100 ppb.

The present process thus makes it possible to purify 2,3,3,3-tetrafluoro-1-propene. Advantageously, the content of at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) in the stream comprising 2,3,3,3-tetrafluoro-1-propene, obtained in step b) of the present purification process, is less than the content of that or those in said first composition. For example, the content of any one of the compounds may be reduced by 50%, advantageously by 75%, preferably by 90%, in particular by 95% and more particularly by 98%. Advantageously, the content of at least two, at least three, at least four, at least five, at least six or of all of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) may be reduced by 50%, advantageously by 75%, preferably by 90%, in particular by 95% and more particularly by 98%. Preferably, the content of 3,3,3-trifluoropropene (1243zf) and/or trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and/or optionally or not at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E) may be reduced by 50%, advantageously by 75%, preferably by 90%, in particular by 95% and more particularly by 98%.

The contents are expressed as weight percentages.

Preferably, the stream comprising 2,3,3,3-tetrafluoro-1-propene obtained in step b) of the present purification process may be free of at least one, at least two, at least three, at least four, at least five, at least six or of all of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) when this or these compounds are present in said first composition. In particular, the stream comprising 2,3,3,3-tetrafluoro-1-propene obtained in step b) of the present purification process may be free of 3,3,3-trifluoropropene (1243zf) and/or of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and/or optionally or not at least one compound chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E). The term “free of” means that the stream comprising 2,3,3,3-tetrafluoro-1-propene comprises less than 50 ppm, advantageously less than 20 ppm and preferably less than 10 ppm of the compound under consideration on the basis of the total weight of the stream.

According to a preferred embodiment, said first composition used in step a) of the present process may be purified before being used. Specifically, if said first composition comprises impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene and optionally heavy impurities, the process may comprise, prior to step a), the following steps:

-   -   i′) implementation or provision of a composition comprising         2,3,3,3-tetrafluoro-1-propene, impurities with a boiling point         below the boiling point of 2,3,3,3-tetrafluoro-1-propene, and at         least one of the compounds chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf), and optionally heavy         impurities; preferably, 2,3,3,3-tetrafluoro-1-propene,         impurities with a boiling point below the boiling point of         2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one of the compounds chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and         optionally heavy impurities;     -   ii′) distillation of said composition from step i) to remove, at         the top of the column, impurities with a boiling point below the         boiling point of 2,3,3,3-tetrafluoro-1-propene and to form a         first stream comprising 2,3,3,3-tetrafluoro-1-propene and at         least one of the compounds chosen from the group consisting of         chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf), and optionally heavy         impurities, recovered at the bottom of the distillation column;         advantageously, the first stream comprises         2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one of the compounds chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E);     -   iii′) optionally, distillation of said first stream recovered at         the bottom of the distillation column in step ii′) to recover,         at the top of the column, a second stream comprising         2,3,3,3-tetrafluoro-1-propene and at least one of the compounds         chosen from the group consisting of chloromethane (40),         1,1-difluoroethane (152a), chloropentafluoroethane (115),         1,1,1,2-tetrafluoroethane (134a),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf), and, at the bottom of the         distillation column, a stream comprising the heavy impurities;         advantageously, the second stream comprises         2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one of the compounds chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E);     -   said at first stream recovered in step ii′) or said second         stream recovered in step iii′) corresponds to said first         composition used in step a).

Said impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene may be trifluoromethane (F23), monofluoromethane (F41), difluoromethane (F32), pentafluoroethane (F125), 1,1,1-trifluoroethane (F143a), trifluoropropyne or 1-chloro-pentafluoroethane (F115). The heavy impurities may contain, for example, 1,1,1,3,3,3-hexafluoropropane (236fa), 1,1,1,2,3,3-hexafluoropropane (236ea), 1,1,1,2,3,3,3-heptafluoropropane (227ca), cis-1,3,3,3-tetrafluoro-1-propene (1234ze-Z), and dimers or trimers derived from one of the compounds present in the composition or the stream under consideration, for example C4 or C5 hydrocarbons such as hexafluorobutene (1336), heptafluorobutene (1327), octafluorobutane (338), nonafluoropentene (1429) or heptafluoropentene (1447).

According to a second aspect, the present invention provides a process for producing 2,3,3,3-tetrafluoro-1-propene. In addition, this process may include the purification thereof. Thus, the present invention provides a process for producing 2,3,3,3-tetrafluoro-1-propene, comprising the steps of:

-   -   A) fluorination in the presence of a catalyst of a compound of         formula CX(Y)₂−CX(Y)_(m)−CH_(m)XY (I) in which X and Y         independently represent H, F or Cl and m=0 or 1; and/or         fluorination in the presence of a catalyst of a compound of         formula (CX_(n)Y_(3−n))CH_(p)X_(1−p)CH_(m)X_(2−m) (II) in which         X is, independently of each other, Cl, F, I or Br; Y is,         independently of each other, H, Cl, F, I or Br; n is 1, 2 or 3;         and m is 0, 1 or 2; and p is 0 or 1;     -   B) recovery of a stream comprising 2,3,3,3-tetrafluoro-1-propene         and at least one of the compounds chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf); advantageously, a stream         comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene         (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and         optionally or not at least one of the compounds chosen from the         group consisting of chloromethane (40), 1,1-difluoroethane         (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane         (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E);     -   C) implementation of the process for purifying         2,3,3,3-tetrafluoro-1-propene according to the present invention         using the stream recovered in step B).

According to a preferred embodiment, the process for producing 2,3,3,3-tetrafluoro-1-propene comprising the steps of:

-   -   A) fluorination in the presence of a catalyst of a compound of         formula CX(Y)₂−CX(Y)_(m)−CH_(m)XY (I) in which X and Y         independently represent H, F or Cl and m=0 or 1; and/or         fluorination in the presence of a catalyst of a compound of         formula (CX_(n)Y_(3−n))CH_(p)X_(1−p)CH_(m)X_(2−m) (II) in which         X is, independently of each other, Cl, F, I or Br; Y is,         independently of each other, H, Cl, F, I or Br; n is 1, 2 or 3;         and m is 0, 1 or 2; and p is 0 or 1;     -   B) recovery of a stream comprising 2,3,3,3-tetrafluoro-1-propene         and at least one of the compounds chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),         trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and         3,3,3-trifluoropropene (1243zf); preferably, a stream comprising         2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf),         trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or         not at least one of the compounds chosen from the group         consisting of chloromethane (40), 1,1-difluoroethane (152a),         chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a)         and trans-1,2,3,3,3-pentafluoropropene (1225ye-E);     -   C) implementation of the process for purifying         2,3,3,3-tetrafluoro-1-propene using the stream recovered in         step B) and comprising the steps of:         -   a) placing said first composition in contact with at least             one organic extracting agent to form a second composition;         -   b) extractive distillation of said second composition to             form:             -   i) a third composition comprising said organic                 extracting agent and at least one of the compounds                 chosen from the group consisting of chloromethane (40),                 1,1-difluoroethane (152a), chloropentafluoroethane                 (115), 1,1,1,2-tetrafluoroethane (134a),                 trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),                 trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and                 3,3,3-trifluoropropene (1243zf); preferably, a third                 composition comprising said organic extracting agent,                 3,3,3-trifluoropropene (1243zf),                 trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and                 optionally or not at least one of the compounds chosen                 from the group consisting of chloromethane (40),                 1,1-difluoroethane (152a), chloropentafluoroethane                 (115), 1,1,1,2-tetrafluoroethane (134a) and                 trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and             -   ii) a stream comprising 2,3,3,3-tetrafluoro-1-propene;         -   c) recovery and separation of said third composition to form             a stream comprising said organic extracting agent and a             stream comprising said at least one of the compounds chosen             from the group consisting of chloromethane (40),             1,1-difluoroethane (152a), chloropentafluoroethane (115),             1,1,1,2-tetrafluoroethane (134a),             trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E),             trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and             3,3,3-trifluoropropene (1243zf); preferably, a stream             comprising said organic extracting agent and a stream             comprising 3,3,3-trifluoropropene (1243zf),             trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and             optionally or not at least one of the compounds chosen from             the group consisting of chloromethane (40),             1,1-difluoroethane (152a), chloropentafluoroethane (115),             1,1,1,2-tetrafluoroethane (134a) and             trans-1,2,3,3,3-pentafluoropropene (1225ye-E).

Preferably, the stream comprising said organic extracting agent is recycled into step a).

According to a particular embodiment, the stream recovered in step B) of the process for producing 2,3,3,3-tetrafluoro-1-propene may comprise hydrofluoric acid. In this case, prior to step C), the stream recovered in step B) may undergo a preliminary distillation B1′) to remove HF at the bottom of the distillation column. A stream comprising 2,3,3,3-tetrafluoro-1-propene and at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) is recovered at the top the distillation column, preferably a stream comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E). The latter stream recovered at the top of the distillation column is then subjected to step C) of the process for producing 2,3,3,3-tetrafluoro-1-propene.

According to a particular embodiment, the stream recovered in step B) of the process for producing 2,3,3,3-tetrafluoro-1-propene may comprise impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene. In this case, prior to step C), the stream recovered in step B) may undergo a preliminary distillation B2′), optionally subsequent to step B1′), to remove, at the top of the distillation column, said impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene and to form a first stream comprising 2,3,3,3-tetrafluoro-1-propene and at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) recovered at the bottom of the distillation column; preferably, a stream comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E). The latter stream recovered at the bottom of the distillation column is then subjected to step C) of the process for producing 2,3,3,3-tetrafluoro-1-propene.

According to a particular embodiment, the stream recovered in step B) of the process for producing 2,3,3,3-tetrafluoro-1-propene may comprise heavy impurities. In this case, prior to step C), the stream recovered in step B) may undergo a preliminary distillation B3′), optionally subsequent to step B1′) and/or B2′), to remove, at the bottom of the distillation column, said heavy impurities; and to form a first stream comprising 2,3,3,3-tetrafluoro-1-propene and at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), trans-1,2,3,3,3-pentafluoropropene (1225ye-E) and 3,3,3-trifluoropropene (1243zf) recovered at the top of the distillation column; preferably, a first stream comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E). The latter stream recovered at the top of the distillation column is then subjected to step C) of the process for producing 2,3,3,3-tetrafluoro-1-propene.

According to a particular embodiment, the stream recovered in step B) of the process for producing 2,3,3,3-tetrafluoro-1-propene may also comprise HCl. The hydrochloric acid may be recovered by distillation before or after step B1′, independently of the other steps of the process.

More particularly, step A) is performed using 1,1,2,3-tetrachloropropene, 2,3,3,3-tetrachloropropene, 1,1,3,3-tetrachloropropene, 1,3,3,3-tetrachloropropene, 1,1,1,2,3-pentachloropropane, 1,1,1,3,3-pentachloropropane, 1,1,2,2,3-pentachloropropane, 1,2-dichloro-3,3,3-trifluoropropane, 2-chloro-2,3,3,3-tetrafluoropropane, 1,1,1,2,2-pentafluoropropane, 1-chloro-1,3,3,3-tetrafluoropropane and 1,1,1,3,3-pentafluoropropane, preferably using 1,1,1,2,3-pentachloropropane, 1,1,2,3,tetrachloropropene, 1,1,1,2,2-pentafluoropropane and/or 2-chloro-3,3,3-trifluoro-1-propene; in particular using 1,1,1,2,3-pentachloropropane (240 db).

FIG. 1a schematically represents a simplified scheme of a device for performing a process for purifying 2,3,3,3-tetrafluoro-1-propene according to a particular embodiment of the invention. The mixture derived from the fluorination reaction, in the presence of a catalyst, a compound of formula (CX_(n)Y_(3−n))CHXCH_(m+1)X_(2−m) (I) and/or catalytic fluorination, in the presence of a catalyst, a compound of formula (CX_(n)Y_(3−n))CH_(p)X_(1−p)=CH_(m)X_(2−m) (II) is obtained in 1. In this particular embodiment, the mixture comprises 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally at least one of the compounds chosen from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene and heavy impurities. The mixture is transferred into a distillation column 2 via pipe 3. Impurities are recovered at the top of distillation column 2 and conveyed via pipe 5 to an incinerator or a purification device 15. The residue obtained at the bottom of the distillation column and comprising the other constituents of the mixture is conveyed to a second distillation column 6 via pipe 4. The distillation performed in 6 is directed toward separating the heavy impurities from the other constituents of the mixture. The distillation operating conditions are thus suitable for this purpose. The heavy impurities are recovered at the bottom of the distillation column 8 and the other constituents are recovered at the top of the distillation column and conveyed to the extractive distillation column 9 via pipe 7. The extractive distillation performed in 9 is directed toward separating 2,3,3,3-tetrafluoro-1-propene from the other constituents of the mixture mentioned above. The extractive distillation device 9 is fed with the organic extracting agent 17 chosen according to the method described in the present patent application. 2,3,3,3-Tetrafluoro-1-propene is recovered at the top of the extractive distillation column 9 and stored or purified in 10 via pipe 11. The mixture recovered at the bottom of the extractive distillation device 9 a specially comprises the organic extracting agent 17, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally at least one of the following compounds: chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E). The mixture recovered at the bottom of the extractive distillation device 9 is conveyed via pipe at 12 to a distillation device 13 which is directed toward separating the organic extracting agent from the other compounds present. The organic extracting agent is recovered at the bottom of the distillation device and recycled via pipe 16 to the extractive distillation device 9. The compounds recovered at the top of the distillation device 13 are conveyed via pipe 14 to pipe 5 to be incinerated or purified in 15.

The mixture provided in 1 may be free of impurities with a boiling point below that of 2,3,3,3-tetrafluoro-1-propene. In this case, as illustrated in FIG. 1b , the mixture 1 is conveyed via pipe 3 to the distillation column 6 to be processed as explained above in relation with FIG. 1a . In another particular embodiment illustrated in FIG. 1c , the mixture 1 may be free of impurities with a boiling point below that of 2,3,3,3-tetrafluoro-1-propene and of heavy impurities. In this case, the mixture is conveyed directly to the extractive distillation column 9 to be processed therein as explained above in relation with FIG. 1 a.

FIG. 2 schematically illustrates a device for performing a process for producing 2,3,3,3-tetrafluoropropene according to a particular embodiment of the present invention. Hydrofluoric acid 21 is placed in contact with 1,1,1,2,3-pentachloropropane (240db) 22 in a reactor 23. The mixture obtained comprises HF, HCl, 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one of the following compounds: chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and optionally or not heavy impurities or impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene. The mixture is recovered at the reactor outlet and conveyed to a distillation column 25 via pipe 24. The stream obtained at the bottom of the distillation column comprising HF and optionally heavy impurities is conveyed to the purification device 27 via pipe 26 to purify HF which will optionally be recycled in 23. The other constituents of the mixture are conveyed via pipe 28 to a purification device 29 for purifying 2,3,3,3-tetrafluoro-1-propene. The purification device 29 may be any of the devices illustrated in FIGS. 1a -1 b.

The catalyst used in the present process for producing 2,3,3,3-tetrafluoropropene may be based, for example, on a metal comprising a transition metal oxide or a derivative or a halide or an oxyhalide of such a metal. Mention may be made, for example, of FeCl₃, chromium oxyfluoride, chromium oxides (optionally subjected to fluorination treatments) and chromium fluorides, and mixtures thereof. Other possible catalysts are catalysts supported on carbon, antimony-based catalysts, and aluminum-based catalysts (for example AlF₃ and Al₂O₃, aluminum oxyfluoride and aluminum fluoride).

Use may be made in general of a chromium oxyfluoride, an aluminum fluoride or oxyfluoride, or an optionally supported catalyst containing a metal such as Cr, Ni, Fe, Zn, Ti, V, Zr, Mo, Ge, Sn, Pb, Mg or Sb.

Reference may be made in this respect to WO 2007/079431 (on page 7, lines 1-5 and 28-32) and EP 939071 (paragraph [0022]), WO 2008/054781 (on page 9, line 22 to page 10, line 34) and WO 2008/040969 (claim 1), to which reference is expressly made.

The catalyst is more particularly preferably chromium-based and it is more particularly a mixed catalyst comprising chromium.

According to one embodiment, a mixed catalyst comprising chromium and nickel is used. The Cr/Ni mole ratio (on the basis of the metal element) is generally from 0.5 to 5, for example from 0.7 to 2, for example about 1. The catalyst may contain from 0.5% to 20% by weight of nickel.

The metal may be present in metallic form or in the form of a derivative, for example an oxide, halide or oxyhalide. These derivatives are preferably obtained by activation of the catalytic metal.

The support is preferably constituted with aluminum, for example alumina, activated alumina or aluminum derivatives, such as aluminum halides and aluminum oxyhalides, for example described in U.S. Pat. No. 4,902,838, or obtained via the activation process described above.

The catalyst may comprise chromium and nickel in an activated or unactivated form, on a support which has optionally been subjected to activation.

Reference may be made to WO 2009/118628 (especially on page 4, line 30 to page 7, line 16), to which reference is expressly made herein.

Another preferred embodiment is based on a mixed catalyst containing chromium and at least one element chosen from Mg and Zn. The atomic ratio of Mg or Zn/Cr is preferably from 0.01 to 5.

Before its use, the catalyst is preferably subjected to activation with air, oxygen or chlorine and/or with HF.

The catalyst is preferably subjected to activation with air or oxygen and HF at a temperature from 100 to 500° C., preferably from 250 to 500° C. and more particularly from 300 to 400° C. The activation time is preferably from 1 to 200 hours and more particularly from 1 to 50 hours.

This activation may be followed by a final fluorination activation step in the presence of an oxidizing agent, HF and organic compounds.

The HF/organic compounds mole ratio is preferably from 2 to 40 and the oxidizing agent/organic compounds mole ratio is preferably from 0.04 to 25. The temperature of the final activation is preferably from 300 to 400° C. and its duration is preferably from 6 to 100 hours.

The gas-phase fluorination reaction may be performed:

-   -   with an HF/compound of formula (I) and/or (II) mole ratio from         3:1 to 150:1, preferably from 4:1 to 125:1 and more particularly         preferably from 5:1 to 100:1;     -   with a contact time from 3 to 100 seconds, preferably 4 to 75         seconds and more particularly 5 to 50 seconds (volume of         catalyst divided by the total entering stream, adjusted to the         operating temperature and pressure);     -   at a pressure ranging from atmospheric pressure to 20 bar,         preferably from 2 to 18 bar and more particularly from 3 to 15         bar;     -   at a temperature (temperature of the catalytic bed) from 200 to         450° C., preferably from 250 to 400° C. and more particularly         from 280 to 380° C.

The duration of the reaction step is typically from 10 to 8000 hours, preferably from 50 to 5000 hours and more particularly preferably from 70 to 1000 hours.

An oxidizing agent, preferably oxygen, may optionally be added during the fluorination reaction. The oxygen/organic compounds mole ratio may be from 0.005 to 2, preferably from 0.01 to 1.5. Oxygen may be introduced in pure form or in the form of air or an oxygen/nitrogen mixture. Oxygen may also be replaced with chlorine.

Method for Selecting the Organic Extracting Agent

The selection of the organic extracting agent is determined by using the Cosmo-RS model implemented in the COSMOTHERM software. For this selected binary couple, a separation factor is calculated for each of the solvents studied via the following equation: S_(1,2)=(γ_(1,S)*P1)/γ_(2,S)*P2) in which

-   -   γ_(1,S) represents the activity coefficient of the first         compound 1 in the organic extracting agent under consideration         at infinite dilution,     -   P1 represents the saturating vapor pressure of the first         compound 1,     -   γ_(2,S) represents the activity coefficient of the second         compound 2 of the binary couple in the organic extracting agent         under consideration at infinite dilution,     -   P2 represents the saturating vapor pressure of the second         compound.

An absorption capacity is also calculated for each of the solvents studied and for a binary couple (1,2) under consideration. The absorption capacity is calculated via the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of the second compound of the binary couple under consideration in said organic extracting agent studied at infinite dilution. The calculations are repeated for each organic extracting agent studied. Minimum separation factor and absorption capacity values are identified so as to allow a sufficient separation between the first compound and the second compound of the binary couple (1,2) under consideration. The saturating vapor pressure is considered for a temperature of 25° C.

Example

To purify 2,3,3,3-tetrafluoro-1-propene, the binary couple 2,3,3,3-tetrafluoro-1-propene/3,3,3-trifluoropropene (1243zf) and the binary couple 2,3,3,3-tetrafluoro-1-propene/trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) were considered to select the organic extracting agent. On the basis of the information obtained by the Cosmo-RS model, the solvents given in table 1 below were tested for the extractive distillation of a mixture comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf) and trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E).

TABLE 1 capacity and separation factor of the organic extracting agent (1234yf/ (1234yf/ (1234yf/ (1234yf/ Organic 1243zf) 1243zf) 1234zeE) 1234zeE) extracting absorption separation absorption separation agent capacity factor capacity factor Dimethoxy- 1.19 1.44 1.37 1.95 methane Isopropyl 1.10 1.42 1.42 2.15 acetate Dioxane 0.92 1.59 1.09 2.24 Trimethoxy- 1.11 1.54 1.28 2.11 methane 1,3-Dioxane 0.95 1.64 1.09 2.23 n-Butyl acetate 1.05 1.41 1.35 2.14 1-Ethoxy-2- 0.85 1.45 1.12 2.27 propanol Hexanal 0.93 1.43 1.09 1.98

The results were confirmed using a mixture comprising 92.0% by weight of 2,3,3,3-tetrafluoro-1-propene, 7.5% by weight of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and 0.5% by weight of 3,3,3-trifluoropropene (1243zf) relative to the total weight of the mixture of the three compounds. The rest of the composition is formed by the organic extracting agent tested. 

1.-15. (canceled)
 16. A process for purifying 2,3,3,3-tetrafluoro-1-propene (1234yf) using a first composition comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), said process comprising: a) placing said first composition in contact with at least one organic extracting agent to form a second composition; b) distilling said second composition by extractive distillation to form: i) a third composition comprising said organic extracting agent, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene(1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E); and ii) a stream comprising 2,3,3,3-tetrafluoro-1-propene; c) recovering and separating said third composition to form a stream comprising said organic extracting agent and a stream comprising 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).
 17. The process as claimed in claim 16, wherein said organic extracting agent comprises a solvent selected from the group consisting of hydrocarbon, halohydrocarbon, alcohol, ketone, amine, ester, ether, aldehyde, nitrile, carbonate, thioalkyl, amide and heterocycle; or said organic extracting agent comprises difluoroethylsilane, triethylfluorosilane or perfluorobutanoic acid.
 18. The process as claimed in claim 16, wherein the organic extracting agent has a boiling point of between 10 and 150° C.
 19. The process as claimed in claim 16, wherein said organic extracting agent has a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/(γ_(2,S)*P2) wherein γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution; P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene; γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) or trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution; and P2 represents the saturating vapor pressure of 3,3,3-trifluoropropene (1243zf) or trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E).
 20. The process as claimed in claim 16, wherein said organic extracting agent has an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) or of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution.
 21. The process as claimed in claim 16, wherein said organic extracting agent has a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/(γ_(2,S)*P2) wherein γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene, γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution; and P2 represents the saturating vapor pressure of 3,3,3-trifluoropropene (1243zf); and said organic extracting agent has a separation factor S_(1,2) of greater than or equal to 1.1, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/(γ_(2,S)*P2) wherein γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoro-1-propene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoro-1-propene, γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution and P2 represents the saturating vapor pressure of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E).
 22. The process as claimed in claim 16, wherein said organic extracting agent has an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) wherein γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution; and said organic extracting agent has an absorption capacity C_(2,S) of greater than or equal to 0.20, said absorption capacity being calculated by the formula C_(2,S)=1/(γ_(2,S)) in which γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution.
 23. The process as claimed in claim 16, wherein said first composition is an azeotropic or quasi-azeotropic composition comprising 2,3,3,3-tetrafluoro-1-propene, trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E), 3,3,3-trifluoropropene (1243zf) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).
 24. The process as claimed in claim 16, wherein said organic extracting agent is selected from the group consisting of 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, n-propyl formate, 1,2-dimethoxyethane, isopropyl acetate, 2-methylbutanal, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 1-methylpiperazine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate, and 1-propoxy-2-propanol.
 25. The process as claimed in claim 16, further comprising recovering the stream comprising 2,3,3,3-tetrafluoro-1-propene formed in step b), wherein said stream is free of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and/or of 3,3,3-trifluoropropene (1243zf) and/or of at least one of the compounds selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E).
 26. The process as claimed in claim 16, wherein said first composition comprises impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene and optionally heavy impurities, and the process further comprises, prior to step a): i′) using a composition comprising 2,3,3,3-tetrafluoro-1-propene, impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and optionally heavy impurities; ii′) distilling said composition from step i) to remove, at the top of the column, impurities with a boiling point below the boiling point of 2,3,3,3-tetrafluoro-1-propene and to form a first stream comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and optionally heavy impurities, recovered at the bottom of the distillation column; iii′) optionally, distilling said first stream recovered at the bottom of the distillation column in step ii′) to recover, at the top of the column, a second stream comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E), and, at the bottom of the distillation column, a stream comprising the heavy impurities; wherein said first stream recovered in step ii′) or said second stream recovered in step iii′) corresponds to said first composition used in step a).
 27. A process for producing and purifying 2,3,3,3-tetrafluoro-1-propene, comprising: A) fluorination in the presence of a catalyst for a compound of formula (I) CX(Y)₂−CX(Y)_(m)−CH_(m)XY wherein X and Y independently represent a hydrogen, fluorine or chlorine atom and m=0 or 1 and/or fluorination in the presence of a catalyst for a compound of formula (CX_(n)Y_(3−n)) CH_(p)X_(1−p)CH_(m)X_(2−m) (II) wherein X is, independently of each other, Cl, F, I or Br; Y is, independently of each other, H, Cl, F, I or Br; n is 1, 2 or 3; and m is 0, 1 or 2; and p is 0 or 1; B) recovering a stream comprising 2,3,3,3-tetrafluoro-1-propene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and optionally or not at least one compound selected from the group consisting of chloromethane (40), 1,1-difluoroethane (152a), chloropentafluoroethane (115), 1,1,1,2-tetrafluoroethane (134a) and trans-1,2,3,3,3-pentafluoropropene (1225ye-E); C) implementing the process as claimed in claim 16 using the stream recovered in step B).
 28. A composition comprising 2,3,3,3-tetrafluoropropene, 3,3,3-trifluoropropene (1243zf), trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) and an organic extracting agent having: a separation factor S_(1,2) of greater than or equal to 1.40, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/(γ_(2,S)*P2) wherein γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoropropene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoropropene, γ_(2,S) represents the activity coefficient of 3,3,3-trifluoropropene (1243zf) in said organic extracting agent at infinite dilution, P2 represents the saturating vapor pressure of 3,3,3-trifluoropropene (1243zf) and a separation factor S_(1,2) of greater than or equal to 1.40, said separation factor being calculated by the formula S_(1,2)=(γ_(1,S)*P1)/(γ_(2,S)*P2) in which γ_(1,S) represents the activity coefficient of 2,3,3,3-tetrafluoropropene in said organic extracting agent at infinite dilution, P1 represents the saturating vapor pressure of 2,3,3,3-tetrafluoropropene, γ_(2,S) represents the activity coefficient of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E) in said organic extracting agent at infinite dilution, P2 represents the saturating vapor pressure of trans-1,3,3,3-tetrafluoro-1-propene (1234ze-E).
 29. The composition as claimed in claim 28, wherein the organic extracting agent is selected from the group consisting of acetaldehyde, methyl formate, 2-methoxy-1-propene, 1,2-epoxypropane, ethoxyethene, dimethoxymethane, 1-chloro-1,2,2-trifluoropropane, 3-chloro-1,1,1-trifluoropropane, ethanedial, 2-chloro-1,1,1,3-tetrafluoropropane, propanone, methyl acetate, 4-methoxy-2-methyl-2-butanethiol, difluorodiethylsilane, isobutanal, isopropyl formate, methylglyoxal, 2,3-dichloro-1,1,1-trifluoropropane, ethyl acetate, butanone, n-propyl formate, 1,3-dichloro-1,1,2-trifluoropropane, 1,1-dichloro-2,2,3-trifluoropropane, 1,2-dimethoxyethane, 1,3-dichloro-1,2,2-trifluoropropane, isopropyl acetate, diethyl sulfide, 1,3-dichloro-1,2,3-trifluoropropane, 2-methylbutanal, 2-allyloxyethanol, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, pyridine, n-methylmorpholine, 4-methyl-2-pentanone, butyronitrile, 1-methoxy2-propanol, diethyl carbonate, n-butyl acetate, 2-hexanone, 5-hexen-2-one, 2-methoxy1-propanol, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 2-ethoxy-1-propanol, 1-methylpiperazine, n-ethylmorpholine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methyl hexanoate, 2-propoxyethanol and 1-propoxy-2-propanol.
 30. The composition as claimed in claim 28, wherein said organic extracting agent is selected from the group consisting of 2-methoxy-1-propene,1,2-epoxypropane, ethoxyethene, dimethoxymethane, methyl acetate, isobutanal, isopropyl formate, ethyl acetate, butanone, n-propyl formate, 1,2-dimethoxyethane, isopropyl acetate, 2-methylbutanal, ethyl propionate, 1,2-dimethoxypropane, dioxane, 3-pentanone, 2-pentanone, trimethoxymethane, 1,3-dioxane, 3,3-dimethyl-2-butanone, 4-methyl-2-pentanone, diethyl carbonate, n-butylacetate, 2-hexanone, 5-hexen-2-one, 1-ethoxy-2-propanol, hexanal, 2-(dimethylamino)ethanol, 2-methylpyrazine, 1-methylpiperazine, valeronitrile, 4-methyl-2-hexanone, 1-methoxy-2-acetoxypropane, 2,6-dimethylmorpholine, methylhexanoate and 1-propoxy-2-propanol. 